RU2002115294A - METHOD FOR REMOVING SILICON ODOR - Google Patents

METHOD FOR REMOVING SILICON ODOR

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Publication number
RU2002115294A
RU2002115294A RU2002115294/04A RU2002115294A RU2002115294A RU 2002115294 A RU2002115294 A RU 2002115294A RU 2002115294/04 A RU2002115294/04 A RU 2002115294/04A RU 2002115294 A RU2002115294 A RU 2002115294A RU 2002115294 A RU2002115294 A RU 2002115294A
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Russia
Prior art keywords
solvent
adsorbent
silicone
approximately
silicone solvent
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Application number
RU2002115294/04A
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Russian (ru)
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RU2250278C2 (en
Inventor
Роберт Джеймс ПЕРРИ
Джон Алфред КИЛГУР
Стивен Б. ДОРН
Original Assignee
Дженерал Электрик Компани
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Priority claimed from US09/437,962 external-priority patent/US6312476B1/en
Application filed by Дженерал Электрик Компани filed Critical Дженерал Электрик Компани
Publication of RU2002115294A publication Critical patent/RU2002115294A/en
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Publication of RU2250278C2 publication Critical patent/RU2250278C2/en

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Claims (18)

1. Способ устранения зловонных элементов из силиконового растворителя для сухой химической чистки, включающий контакт силиконового растворителя с адсорбентом, и отделения силиконового растворителя от адсорбента.1. A method of eliminating stinking elements from a silicone solvent for dry dry cleaning, comprising contacting the silicone solvent with the adsorbent, and separating the silicone solvent from the adsorbent. 2. Способ по п.1, в котором указанный способ является периодическим.2. The method according to claim 1, wherein said method is batch. 3. Способ по п.1, в котором указанный способ является непрерывным.3. The method according to claim 1, wherein said method is continuous. 4. Способ по п.2, в котором приблизительно 100 вес.ч. силикона подвергают контакту приблизительно со 100 вес.ч. абсорбента.4. The method according to claim 2, in which approximately 100 parts by weight silicone is contacted with approximately 100 parts by weight absorbent. 5. Способ по п.2, в котором растворитель находится в контакте с адсорбентом в течение приблизительно от 0,1 до 6 ч.5. The method according to claim 2, in which the solvent is in contact with the adsorbent for about 0.1 to 6 hours 6. Способ по п.2, в котором растворитель находится в контакте с адсорбентом при температуре, составляющей приблизительно от 10 до 100°С.6. The method according to claim 2, in which the solvent is in contact with the adsorbent at a temperature of approximately 10 to 100 ° C. 7. Способ по п.3, в котором силиконовый растворитель подвергают контакту с адсорбентом при соотношении, составляющем приблизительно от 10 вес.ч. растворителя приблизительно до 1 вес.ч. адсорбента.7. The method according to claim 3, in which the silicone solvent is contacted with an adsorbent in a ratio of approximately 10 parts by weight. solvent to about 1 parts by weight adsorbent. 8. Способ по п.3, в котором растворитель находится в контакте с адсорбентом в течение приблизительно от 0,1 до 6 ч.8. The method according to claim 3, in which the solvent is in contact with the adsorbent for about 0.1 to 6 hours 9. Способ по п.3, в котором растворитель находится в контакте с адсорбентом при температуре, составляющей приблизительно от 10 до 100°С.9. The method according to claim 3, in which the solvent is in contact with the adsorbent at a temperature of approximately 10 to 100 ° C. 10. Способ по п.1, в котором адсорбент означает гранулированный активированный уголь, 4А или 13Х молекулярные сита.10. The method according to claim 1, in which the adsorbent means granular activated carbon, 4A or 13X molecular sieves. 11. Способ по п.1, в котором растворитель означает линейный или разветвленный летучий силоксановый растворитель формулы11. The method according to claim 1, in which the solvent means a linear or branched volatile siloxane solvent of the formula M2+y+2zDxTyQz, M 2 + y + 2z D x T y Q z, в которой М означает R 1 3 SiO1/2;in which M means R 1 3 SiO 1/2 ; D означает R 2 2 SiO2/2;D means R 2 2 SiO 2/2 ; Т означает R3SiO3/2;T means R 3 SiO 3/2 ; Q означает SiO4/2,Q means SiO 4/2 , каждый из R1, R2 и R3 независимо означает одновалентный углеводородный радикал;each of R 1 , R 2 and R 3 independently means a monovalent hydrocarbon radical; каждый из х и у означает целое число, при этом 0≤х≤10, 0≤у1≤0 и 0≤z≤10.each of x and y means an integer, with 0≤x≤10, 0≤y1≤0 and 0≤z≤10. 12. Способ по п.1, в котором растворитель означает циклический силоксан формулы12. The method according to claim 1, in which the solvent means a cyclic siloxane of the formula
Figure 00000001
Figure 00000001
в которой каждый из R5, R6, R7 и R8 независимо означает одновалентную углеводородную группу;in which each of R 5 , R 6 , R 7 and R 8 independently means a monovalent hydrocarbon group; каждый из а и b представляет целые числа, при этом 0≤а≤10 и 0≤b≤10, при условии, что 3≤(а + b)≤10.each of a and b represents integers, with 0≤a≤10 and 0≤b≤10, provided that 3≤ (a + b) ≤10.
13. Способ по п.12, в котором циклический силоксан по существу состоит из декаметилциклопентасилоксана.13. The method according to item 12, in which the cyclic siloxane essentially consists of decamethylcyclopentasiloxane. 14. Способ по п.1, в котором зловонные элементы, удаляемые из растворителя, означают пропионовую кислоту, пропионовый альдегид, масляную кислоту или масляный альдегид.14. The method according to claim 1, wherein the malodorous elements removed from the solvent are propionic acid, propionic aldehyde, butyric acid or butyraldehyde. 15. Силиконовый растворитель, обработанный способом по п.1.15. Silicone solvent processed by the method according to claim 1. 16. Адсорбент, применяемый в способе по п.1, в котором указанный адсорбент включает зловонные элементы, выбранные из пропионовой кислоты, пропионового альдегида, масляной кислоты и масляного альдегида.16. The adsorbent used in the method according to claim 1, wherein said adsorbent comprises malodorous elements selected from propionic acid, propionic aldehyde, butyric acid and butyric aldehyde. 17. Способ сухой чистки, включающий (1) чистку изделия в результате проведения следующих стадий: (a) контакт изделия с силиконовым растворителем, и (b) удаление силиконового растворителя, а также (2) обработку силиконового растворителя, удаленного со следующих стадий (a) контакт силиконового растворителя с адсорбентом, и (b) отделение силиконового растворителя от адсорбента.17. A dry cleaning method comprising (1) cleaning the product as a result of the following steps: (a) contacting the product with a silicone solvent, and (b) removing the silicone solvent, and (2) treating the silicone solvent removed from the following steps (a ) contacting the silicone solvent with the adsorbent, and (b) separating the silicone solvent from the adsorbent. 18. Способ по п.17, дополнительно включающий повторное использование обработанного силиконового растворителя на стадии (1).18. The method according to 17, further comprising reusing the treated silicone solvent in step (1).
RU2002115294/04A 1999-11-10 2000-10-23 Method for eliminating of odors from silicones RU2250278C2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US09/437,962 1999-11-10
US09/437962 1999-11-10
US09/437,962 US6312476B1 (en) 1999-11-10 1999-11-10 Process for removal of odors from silicones

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RU2002115294A true RU2002115294A (en) 2003-12-27
RU2250278C2 RU2250278C2 (en) 2005-04-20

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US (1) US6312476B1 (en)
EP (1) EP1242539B1 (en)
KR (1) KR100754551B1 (en)
CN (1) CN1252185C (en)
AT (1) ATE321099T1 (en)
AU (1) AU1227101A (en)
BR (1) BR0015448A (en)
DE (1) DE60026871T2 (en)
DK (1) DK1242539T3 (en)
EG (1) EG22866A (en)
ES (1) ES2260062T3 (en)
GC (1) GC0000210A (en)
HK (1) HK1056190A1 (en)
MX (1) MXPA02004705A (en)
PT (1) PT1242539E (en)
RU (1) RU2250278C2 (en)
TW (1) TWI272329B (en)
WO (1) WO2001034706A1 (en)

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