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SU86796A1 - Installation for drying pulverized or fine-grained fuel by solid heat carrier - Google Patents

Installation for drying pulverized or fine-grained fuel by solid heat carrier

Info

Publication number
SU86796A1
SU86796A1 SU371319A SU371319A SU86796A1 SU 86796 A1 SU86796 A1 SU 86796A1 SU 371319 A SU371319 A SU 371319A SU 371319 A SU371319 A SU 371319A SU 86796 A1 SU86796 A1 SU 86796A1
Authority
SU
USSR - Soviet Union
Prior art keywords
heat carrier
fine
installation
solid heat
fuel
Prior art date
Application number
SU371319A
Other languages
Russian (ru)
Inventor
Ф.Г. Казаринов
Original Assignee
Ф.Г. Казаринов
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 Ф.Г. Казаринов filed Critical Ф.Г. Казаринов
Priority to SU371319A priority Critical patent/SU86796A1/en
Application granted granted Critical
Publication of SU86796A1 publication Critical patent/SU86796A1/en

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  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Drying Of Solid Materials (AREA)

Description

Применение твердого теплоносител , а также отбор и использование сокового пара известны в технике сушки и широко примен ютс  ма практике.The use of solid heat transfer fluid, as well as the selection and use of juice vapor are known in the drying technique and are widely used in practice.

Предлагаема  установка дл  сушки пылевидпого или мелкозернистого топлива твердым теплоносителем отличаетс  от известных тем, что в ней, с целью предварительного нагрева топлива перед сушкой, нрименен теплообменник, через который проходит отработавший теплоноситель в смеси с подлежащим сушке топливом.The proposed plant for drying pulverized or fine-grained fuel with a solid heat carrier differs from the known ones in that, in order to preheat the fuel before drying, a heat exchanger is used, through which the spent heat carrier in mixture with the fuel to be dried passes.

На чертеже показана схема установки.The drawing shows the installation diagram.

Холодный теплоноситель из бункера 16 непрерывно поступает через затвор /7 в загрузочную коробку 18 и нагревательную шахтную печь 19, обогреваемую дымовыми газами из топки 20.Cold coolant from the hopper 16 is continuously fed through the valve / 7 into the loading box 18 and the heating shaft furnace 19, heated by flue gases from the furnace 20.

Гор чий теплоноситель непрерывно выгружаетс  из печи 19 при помощи лоткового разгружател  6 и подаетс  в установленном количестве в сушильную шахту 9. Сюда же подаетс  при помощи дозирующего лопастного питател  2 соответствующее количество предварительно подогреваемого топлива. Пересыпа сь по направл ющим поверхност м сушильной шахты, смесь собираетс  в нижней части шахты 9, откуда лотковым разгружателем / подаетс  на грохот 7.The hot coolant is continuously discharged from the furnace 19 by means of a tray discharger 6 and is supplied in the prescribed amount to the drying shaft 9. Here, the corresponding amount of preheated fuel is supplied by the metering vane feeder 2. Flowing along the guiding surfaces of the drying shaft, the mixture is collected in the lower part of the shaft 9, from where a tray unloader / discharger is fed to the screen 7.

Высушенное топливо собираетс  под грохотом в бункере 13, откуда поступает далее к потребителю по транспортеру 14, питаемому лопастным разгружателем 22.The dried fuel is collected under a screen in a bunker 13, from which it is then supplied to the consumer via a conveyor 14 fed by a paddle unloader 22.

Теплоноситель, имеющий размеры куска 25 мм и освобожденный на грохоте от примеси топлива, тюступает в смесительный бункер 5, куда одновременно из бункера 24 лопастным разгружателем 23 подаетс  холодное сырое топливо. Из бункера 3 смесь подаетс  элеватором 4 в теплообменник 5, представл ющий собой вертикальную шахту с наклонными полками дл  более интенсивного перемешивани  смеси нз холодногоThe heat carrier, having the dimensions of a piece of 25 mm and freed from the thunder of impurities from the fuel, is transferred into a mixing bunker 5, where simultaneously cold raw fuel is fed from the bunker 24 with a paddle unloader 23. From the hopper 3, the mixture is fed by an elevator 4 to the heat exchanger 5, which is a vertical shaft with inclined shelves for more intensive mixing of the mixture from the cold

SU371319A 1947-11-17 1947-11-17 Installation for drying pulverized or fine-grained fuel by solid heat carrier SU86796A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU371319A SU86796A1 (en) 1947-11-17 1947-11-17 Installation for drying pulverized or fine-grained fuel by solid heat carrier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU371319A SU86796A1 (en) 1947-11-17 1947-11-17 Installation for drying pulverized or fine-grained fuel by solid heat carrier

Publications (1)

Publication Number Publication Date
SU86796A1 true SU86796A1 (en) 1949-11-30

Family

ID=48258713

Family Applications (1)

Application Number Title Priority Date Filing Date
SU371319A SU86796A1 (en) 1947-11-17 1947-11-17 Installation for drying pulverized or fine-grained fuel by solid heat carrier

Country Status (1)

Country Link
SU (1) SU86796A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2492397C1 (en) * 2012-04-06 2013-09-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Забайкальский государственный университет" (ФГБОУ ВПО "ЗабГУ") Device for drying bulk materials

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2492397C1 (en) * 2012-04-06 2013-09-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Забайкальский государственный университет" (ФГБОУ ВПО "ЗабГУ") Device for drying bulk materials

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