SU1611215A3 - Method of producing glass spheres - Google Patents
Method of producing glass spheres Download PDFInfo
- Publication number
- SU1611215A3 SU1611215A3 SU4027856A SU4027856A SU1611215A3 SU 1611215 A3 SU1611215 A3 SU 1611215A3 SU 4027856 A SU4027856 A SU 4027856A SU 4027856 A SU4027856 A SU 4027856A SU 1611215 A3 SU1611215 A3 SU 1611215A3
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- fuel
- gas
- combustion chamber
- burner
- mixture
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/10—Forming beads
- C03B19/1005—Forming solid beads
- C03B19/102—Forming solid beads by blowing a gas onto a stream of molten glass or onto particulate materials, e.g. pulverising
- C03B19/1025—Bead furnaces or burners
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
- Glass Melting And Manufacturing (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Pre-Mixing And Non-Premixing Gas Burner (AREA)
Abstract
Description
чентил тор 7, почдухопровод В и газопровод 9 полают горючую СМРСЬОО вторую горслоччую головку 10.Centiel torus 7, air duct B and gas pipeline 9 pour the combustible SMRSSA head 2 10.
Основание 2 каморы вытюлноно открытым , поэтому нижн часть камери 11 сгорани ecTccTBPHiifc i под питьгоаетг. окружа:1)тим , текущим вверх по клиллу 12 между утлом горелки и стенклми иижнс Л част i 1 1 камеры сгорлии . Может быть угтаноп- леи третий ноитил тор дл подачи поз духа по полпухопроподу к оскорашпо 2 камеры II сгорани .The base 2 of the chamber is open, so the lower part of the combustion chamber 11 is ecTccTBPHiifc i under the tap. surroundings: 1) tim, flowing upward through Clíll 12 between the fragile burner and the walls of the burner chamber i 1 1. There may be a third noitil torpedo tori for delivering poses of the spirit along half-dry propane to Oskorashpo 2 combustion chambers II.
Пример 1, Водный раствор борпоЛ кислоты ВПОД1ШИ п реакиим с едким натром и смоти али с гидрированым снликатом иатрнк дл получени раствора, содержпщогг 35 млс. раст- роремного прщегтва, Ч качестве по- .рообразующего вещостча добавл ли мочевину в количестае, прибли:1итольио 2 мае./, pacTBOp« Hiioro вегсествл, и этот р стпор высушивали рлспылсниемExample 1 An aqueous solution of boropoly acid VODODI OTHER with caustic soda and see with hydrogenated solution of sodium for the preparation of a solution containing 35 ml / sec. of uranium in quantity, approx. 1tolio on 2 May /, pacTBOp “Hiioro vegestvl, and this solution were dried with a spray
ИЧПССТНЫХ способом дл 1 ОЛ {еНИН КОМкооОразного исходною продукта.The EICHT method for 1 NL {YNIN COMCOOOR of the original product.
Удобно использпплть комхи со сред ниг1 размером зерен о- 40 до ftO мкм, в зависимости от жоп.г- ого J.o4c-4Horo продукта. Лп.тпп рмсусеш ого исходного пронукга показал с:те;;уюсл1С лри- Р/лизительныо пропорции сне t лпиы:- вс- лес7 и, мае . :It is convenient to use commi with medium nig1 grain size of about -40 to ftO microns, depending on the ass of J. o4c-4Horo product. Lt.tppsy source thru penetration showed with: those ;; uusl1S lri- R / lysitious proportions of sleep t lpiy: - in all 7, and May. :
В() }-рB ()} -р
бориоЛ 1,-ть , }1boriol 1, -t,} 1
(КлПН)(CLP)
.дкий Н.1ТР25, il.DI H.1TP25, il
rivtpnpoii-тиHhjf силикатrivtpnpoii-ti Hhjf silicate
натри 7,05rub 7.05
Получаниы таким о рлпом исходный м-зтгриал поцлпа.;.: ч гпррлку со скоростью 150 кг/ ь поюк-посигель,Getting such a rlp source m-citral ptslpa.;.: H gprlku with a speed of 150 kg / s poyuk-sigel,
,jj
обраиог чпныЛ подачей 250 м /ч природного I пз и 1250 ьотдуха, и 1ТОТ глзовыО поток подх; гал;|. Лоппл- ннтельньп поток иочлухл 11од;1Т ; - и в основание хлмерм торани со гкоро- ). 1 70()(, iiM /ч д.ч пхнл-мллгш пламени , rtt xo/innri o и г орслки, TnKi M olIpanoM, .ичостпо ноч..ухл, п.алнпг -1ОГО и псток-носитель, сое т. плчло пример ю поло П ну .то, что ьспбхоДКМ Ч дл полного (IdpTiUlU, а II CKpymai-jcu A f.-zioiin руОашке 1 дес ть р.п п; ОП11шлл JTO кс.лтич г- по, Г5 по « нтсому примеру дополнитсль)1ыс- Г} по Ht- пользовалн. В р«--тультлте полу0Normal flow of 250 m / h of natural natural gas I pz and 1250 breaths, and 1TOT of the main flow; gal; |. Lopplnntelnp flow and hluhl 11od; 1T; - and at the base hlmerm torani with gkoro). 1 70 () (, iiM / h d.h phnl-mllsh flame, rtt xo / innri o and g orslki, TnKi M olIpanoM,. Hotspopo night..hl, p.alnpg -1OHO and PSK carrier, so m. He gave an example of a polo pnu that it was full for (IdpTiUlU, and II Ckpymai-jcu A f.-zioiin ruOashka 1 ten pp; OP11shll JTO x.ltich go, G5 according to the example add) 1s- Г} by Ht- user. In p «- tultlte semi0
5five
00
5five
00
5five
00
5five
чем высокий выход хорошо сформиро- астичс гранул. Гранулометри полученных гзким образом гранул по- , что ьсе гранулы проход т сквозь сито с размером чейки 250 мкм, более чем 75 мае. проходит сквозь сито с размером чеПки 150 мкм и литаз, 5 мас.% проходит сквозь сито с размером чейки 5 мкм. npH iepito половина гранул проходит скиозь сито с размером чеЛки 100 мкм.the higher yield is well formed granules. The granulometries of the granules obtained in a gzkim way are that all the granules pass through a sieve with a mesh size of 250 µm, more than 75 May. passes through a 150 μm mesh and a lithase sieve; 5 wt.% passes through a 5 μm sieve. The npH iepito half of the granules passes a skios sieve with a mesh size of 100 microns.
В качестве варианта данного примера I3MOCTO борной кислоты использовали буру,As a variation of this example of boric acid I3MOCTO, borax was used,
Пример 2. Комкопый исходный материал, приготовл. нчый, как и в пр мог-е I , поданали в горелку со скоростью 150 кг/ч а поток-носитель, . г кый кпменноугольньп т газом I ьо лухом. горелку подавали 300 л ме 1ноугольного газа и 000 ИУ -/ч воздуха, и тот поток под игали. Тг плотворна способность чгимене; но -о каменноугольного газа состанила ккалУнм и его при- блититпльны состав по объему был следучзпим, ,: СО 6,9; И 52,9; ГН4 29,; иллшминаиты 0,8; 0 0,8; COg 2,1; Nj fi,o. Кромг- того, по , окружающийExample 2. Komkopy source material prepared. The first, as in PROMI I, was fed into the burner at a speed of 150 kg / h and the carrier stream,. gas exchangers with gas I luh. The burner was supplied with 300 l of IU of coal gas and 000 PS - / h of air, and that flow was under the needle. Tg is a literary ability; but -o coal gas was sotated kcalUnm and its nearplit composition of the volume was the following:, CO 6.9; And 52.9; GN4 29; Illshminaity 0.8; 0 0.8; COg 2.1; Nj fi, o. Kromgogo, on, surrounding
г-коростмо iOOO им /ч дл g-korostmo iOOO them / h for
лл .лли п 12,lll, clause 12,
горелку с.burner with
гбразо тниич поздулшой руОгшки, окружпюпоГ флке.ч I :, ш-гход щий из горелкн .gzraz tniich pozdulshoy ruOgshki, surrounded by fluke.h I:, w-going from the burner.
Топлчнч -вочл т ную смесь также по- ддп.члн м-т дп группы горелок, п каж- И которых входило 4 горелки 13, Н из пспомогательимх rpynit горелок подаплли 150 им /ч каменноугольного -ачл и 200 нм /ч воздуха. зон л ncпo oгaтeльныx гсрелок. отстоит ил ; м в срх над основной горелкой 1, а втора группа расположена на 1 м пьппе первой.Topln-inlet mixture is also supplied from the group of burner groups, each of which included 4 burners 13, H from the rpynit burners of 150 km / h of coal and 200 nm / h of air. zones of emergency grelok. stand sludge; m in cpx above the main burner 1, and the second group is located on the 1 m pippa first.
Этот процесс также позвол ет по- лучит -. высокий пыход хорошо с(}юрмн- Р.ИЯН;|;,)Х гранул.This process also allows for -. high pyhod well with (} yurmn- R.IAN; |;,) X granules.
ЛОLO
ФормулFormulas
изобретенииthe invention
Claims (3)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8518680A GB2178024B (en) | 1985-07-24 | 1985-07-24 | Process of and apparatus for producing vitreous beads |
Publications (1)
Publication Number | Publication Date |
---|---|
SU1611215A3 true SU1611215A3 (en) | 1990-11-30 |
Family
ID=10582776
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU4027856A SU1611215A3 (en) | 1985-07-24 | 1986-07-23 | Method of producing glass spheres |
Country Status (10)
Country | Link |
---|---|
CN (1) | CN1017888B (en) |
AU (1) | AU581328B2 (en) |
BE (1) | BE905136A (en) |
CS (1) | CS271337B2 (en) |
ES (2) | ES8800569A1 (en) |
FR (1) | FR2585348B1 (en) |
GB (1) | GB2178024B (en) |
HU (1) | HU212474B (en) |
SU (1) | SU1611215A3 (en) |
ZA (1) | ZA865478B (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8914639D0 (en) * | 1989-06-26 | 1989-08-16 | Shell Int Research | Heat processing of particulate material and apparatus therefor |
CA2186512C (en) * | 1994-04-25 | 2007-01-16 | Richard B. Castle | Compositions comprising fused particulates and methods of making them |
US6254981B1 (en) | 1995-11-02 | 2001-07-03 | Minnesota Mining & Manufacturing Company | Fused glassy particulates obtained by flame fusion |
DE69729225T2 (en) * | 1997-05-22 | 2005-05-19 | Siren Jian | METHOD AND DEVICE FOR RECOVERING ENERGY FROM MILLING AND COMBUSTION |
US6813902B2 (en) * | 2000-11-01 | 2004-11-09 | American Air Liquide, Inc. | Systems and methods for increasing production of spheroidal glass particles in vertical glass furnaces |
CN101633551B (en) * | 2009-09-09 | 2011-08-24 | 中材科技股份有限公司 | Glass ball manufacturing device |
CN103553304B (en) * | 2013-10-31 | 2016-03-09 | 河北勇龙邦大新材料有限公司 | A kind of method and apparatus of inorganic microspheres Fast Sintering |
CA3165336A1 (en) * | 2020-01-24 | 2021-07-29 | Gerhard Olbert | Process of manufacturing hollow spherical glass particles |
CN113754252B (en) * | 2021-09-28 | 2022-11-29 | 陕西科技大学 | Preparation method and production device of large-particle spherical glass |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE521556A (en) * | 1953-07-18 | |||
NL232500A (en) * | 1957-10-22 | |||
US3190737A (en) * | 1960-07-07 | 1965-06-22 | Flex O Lite Mfg Corp | Glass bead furnace and method of making glass beads |
NL289029A (en) * | 1962-03-27 | |||
GB1060234A (en) * | 1964-05-16 | 1967-03-01 | Cataphote Corp | Method and apparatus for manufacturing glass beads |
US3579720A (en) * | 1968-01-04 | 1971-05-25 | Glaverbel | Apparatus for subdividing fluid mass into grains |
IE51461B1 (en) * | 1980-08-15 | 1986-12-24 | Redland Technology Ltd | Method and apparatus for the production of glass beads |
EP0086599A1 (en) * | 1982-02-12 | 1983-08-24 | Redland Technologies Limited | Method and apparatus for the heat processing of particulate materials |
GB2121782B (en) * | 1982-06-08 | 1986-10-22 | Glaverbel | Manufacture of rounded vitreous beads |
-
1985
- 1985-07-24 GB GB8518680A patent/GB2178024B/en not_active Expired
-
1986
- 1986-06-21 ES ES556391A patent/ES8800569A1/en not_active Expired
- 1986-06-23 ES ES556402A patent/ES8706580A1/en not_active Expired
- 1986-07-03 CS CS865039A patent/CS271337B2/en not_active IP Right Cessation
- 1986-07-10 AU AU60036/86A patent/AU581328B2/en not_active Expired
- 1986-07-17 CN CN86104731A patent/CN1017888B/en not_active Expired
- 1986-07-18 BE BE1/011520A patent/BE905136A/en not_active IP Right Cessation
- 1986-07-21 FR FR868610658A patent/FR2585348B1/en not_active Expired - Lifetime
- 1986-07-23 SU SU4027856A patent/SU1611215A3/en active
- 1986-07-23 HU HU863001A patent/HU212474B/en not_active IP Right Cessation
- 1986-07-23 ZA ZA865478A patent/ZA865478B/en unknown
Non-Patent Citations (1)
Title |
---|
Патент GB 2121782, кл. С 03 В 19/10, 1984. * |
Also Published As
Publication number | Publication date |
---|---|
ES8800569A1 (en) | 1987-11-01 |
GB2178024A (en) | 1987-02-04 |
ES556391A0 (en) | 1987-11-01 |
CS503986A2 (en) | 1990-02-12 |
GB2178024B (en) | 1989-08-02 |
HU212474B (en) | 1996-07-29 |
ES556402A0 (en) | 1987-07-01 |
GB8518680D0 (en) | 1985-08-29 |
FR2585348A1 (en) | 1987-01-30 |
AU581328B2 (en) | 1989-02-16 |
CN1017888B (en) | 1992-08-19 |
CN86104731A (en) | 1987-01-21 |
HUT45464A (en) | 1988-07-28 |
FR2585348B1 (en) | 1992-12-04 |
CS271337B2 (en) | 1990-09-12 |
AU6003686A (en) | 1987-01-29 |
BE905136A (en) | 1987-01-19 |
ZA865478B (en) | 1987-03-25 |
ES8706580A1 (en) | 1987-07-01 |
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