RU2015101234A - Способы удаления растворителя из багассы - Google Patents
Способы удаления растворителя из багассы Download PDFInfo
- Publication number
- RU2015101234A RU2015101234A RU2015101234A RU2015101234A RU2015101234A RU 2015101234 A RU2015101234 A RU 2015101234A RU 2015101234 A RU2015101234 A RU 2015101234A RU 2015101234 A RU2015101234 A RU 2015101234A RU 2015101234 A RU2015101234 A RU 2015101234A
- Authority
- RU
- Russia
- Prior art keywords
- bagasse
- organic solvents
- wet
- dried
- guayula
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract 13
- 239000002904 solvent Substances 0.000 title claims abstract 5
- 241000985653 Bagassa Species 0.000 title 1
- 241000609240 Ambelania acida Species 0.000 claims abstract 24
- 239000010905 bagasse Substances 0.000 claims abstract 24
- 239000003960 organic solvent Substances 0.000 claims abstract 16
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims abstract 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims abstract 4
- 230000008020 evaporation Effects 0.000 claims abstract 4
- 238000001704 evaporation Methods 0.000 claims abstract 4
- 238000010438 heat treatment Methods 0.000 claims abstract 4
- 239000004484 Briquette Substances 0.000 claims abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract 2
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
- F26B3/04—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour circulating over or surrounding the materials or objects to be dried
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
- C08C4/00—Treatment of rubber before vulcanisation, not provided for in groups C08C1/00 - C08C3/02
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08H—DERIVATIVES OF NATURAL MACROMOLECULAR COMPOUNDS
- C08H99/00—Subject matter not provided for in other groups of this subclass, e.g. flours, kernels
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
- C08C1/00—Treatment of rubber latex
- C08C1/02—Chemical or physical treatment of rubber latex before or during concentration
- C08C1/04—Purifying; Deproteinising
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/14—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects using gases or vapours other than air or steam, e.g. inert gases
- F26B21/145—Condensing the vapour onto the surface of the materials to be dried
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Treating Waste Gases (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
1. Способ удаления органических растворителей из влажной багассы, включающий:использование некоторого количества влажной багассы, которая содержит до 45 мас. % объединенных органических растворителей и воды (в расчете на общую массу влажной багассы) и не более 0,1 мас. % каучука;нагревание влажной багассы до температуры по меньшей мере 100°C, в результате чего происходит выпаривание органических растворителей;получение высушенной багассы, которая содержит не более 1 мас. % органических растворителей.2. Способ по п. 1, в котором указанную багассу получают из кустарника гуаюла.3. Способ по п. 1 или 2, в котором нагревание проводят в устройстве, выбранном из следующих:i. сушилка, содержащая несколько слоев, в которой нагретый воздух циркулирует через указанные слои устройства и проходит от одного слоя влажной багассы из гуаюлы к другому, в результате чего происходит выпаривание органических растворителей;ii. сушилка, содержащая множество лопастей для перемешивания влажной багассы с нагретым воздухом для выпаривания органических растворителей; илиiii. шнековый экструдер для удаления растворителя,с получением высушенной багассы из гуаюлы, содержащей не более 1 мас. % органических растворителей.4. Способ по п. 1 или 2, дополнительно включающий конденсацию выпаренных органических растворителей и сбор их отдельно от высушенной багассы.5. Способ по п. 1 или 2, дополнительно включающий прессование высушенной багассы в брикет, плотность которого по меньшей мере на 40% выше плотности непрессованной сушеной багассы.6. Способ по п. 1 или 2, в котором объединенные растворители представляют собой ацетон и гексан.
Claims (6)
1. Способ удаления органических растворителей из влажной багассы, включающий:
использование некоторого количества влажной багассы, которая содержит до 45 мас. % объединенных органических растворителей и воды (в расчете на общую массу влажной багассы) и не более 0,1 мас. % каучука;
нагревание влажной багассы до температуры по меньшей мере 100°C, в результате чего происходит выпаривание органических растворителей;
получение высушенной багассы, которая содержит не более 1 мас. % органических растворителей.
2. Способ по п. 1, в котором указанную багассу получают из кустарника гуаюла.
3. Способ по п. 1 или 2, в котором нагревание проводят в устройстве, выбранном из следующих:
i. сушилка, содержащая несколько слоев, в которой нагретый воздух циркулирует через указанные слои устройства и проходит от одного слоя влажной багассы из гуаюлы к другому, в результате чего происходит выпаривание органических растворителей;
ii. сушилка, содержащая множество лопастей для перемешивания влажной багассы с нагретым воздухом для выпаривания органических растворителей; или
iii. шнековый экструдер для удаления растворителя,
с получением высушенной багассы из гуаюлы, содержащей не более 1 мас. % органических растворителей.
4. Способ по п. 1 или 2, дополнительно включающий конденсацию выпаренных органических растворителей и сбор их отдельно от высушенной багассы.
5. Способ по п. 1 или 2, дополнительно включающий прессование высушенной багассы в брикет, плотность которого по меньшей мере на 40% выше плотности непрессованной сушеной багассы.
6. Способ по п. 1 или 2, в котором объединенные растворители представляют собой ацетон и гексан.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201261660971P | 2012-06-18 | 2012-06-18 | |
US61/660,971 | 2012-06-18 | ||
PCT/US2013/046409 WO2013192227A1 (en) | 2012-06-18 | 2013-06-18 | Methods for desolventization of bagasse |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2015101234A true RU2015101234A (ru) | 2016-08-10 |
RU2633580C2 RU2633580C2 (ru) | 2017-10-13 |
Family
ID=49769309
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2015101234A RU2633580C2 (ru) | 2012-06-18 | 2013-06-18 | Способы удаления растворителя из багассы |
Country Status (9)
Country | Link |
---|---|
US (2) | US9562720B2 (ru) |
EP (2) | EP2861655B1 (ru) |
CN (2) | CN105073862B (ru) |
AU (1) | AU2013277296B2 (ru) |
CA (1) | CA2876958C (ru) |
ES (2) | ES2936462T3 (ru) |
MX (1) | MX2014015390A (ru) |
RU (1) | RU2633580C2 (ru) |
WO (1) | WO2013192227A1 (ru) |
Families Citing this family (13)
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WO2013173625A1 (en) | 2012-05-16 | 2013-11-21 | Bridgestone Corporation | Compositions containing purified non-hevea rubber and related purification methods |
WO2013192182A1 (en) | 2012-06-18 | 2013-12-27 | Bridgestone Corporation | Systems and methods for the management of waste associated with processing guayule shrubs to extract rubber |
WO2013192227A1 (en) * | 2012-06-18 | 2013-12-27 | Bridgestone Corporation | Methods for desolventization of bagasse |
CA2876956C (en) | 2012-06-18 | 2021-07-27 | Bridgestone Corporation | Methods for increasing the extractable rubber content of non-hevea plant matter |
WO2015038707A1 (en) | 2013-09-11 | 2015-03-19 | Bridgestone Corporation | Processes for the removal of rubber from tks plant matter |
WO2016044237A1 (en) | 2014-09-18 | 2016-03-24 | Bridgestone Corporation | Extractor and related methods |
JP6557102B2 (ja) * | 2015-09-17 | 2019-08-07 | 日立造船株式会社 | ポリイソプレンの製造方法 |
WO2018079958A1 (ko) * | 2016-10-25 | 2018-05-03 | 엔디티엔지니어링(주) | 건조효율이 개선된 폐열을 활용한 음식물 건조장치 |
US10775105B2 (en) * | 2018-11-19 | 2020-09-15 | Bridgestone Corporation | Methods for the desolventization of bagasse |
US20220056160A1 (en) * | 2018-12-21 | 2022-02-24 | Bridgestone Corporation | Processes For Removing Color Bodies From Guayule |
WO2020132236A1 (en) * | 2018-12-21 | 2020-06-25 | Bridgestone Corporation | Processes for increasing the molecular weight of guayule natural rubber |
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CN114526577B (zh) | 2024-01-30 |
EP2861655A1 (en) | 2015-04-22 |
US9562720B2 (en) | 2017-02-07 |
US10132563B2 (en) | 2018-11-20 |
US20150184933A1 (en) | 2015-07-02 |
CA2876958C (en) | 2021-10-19 |
CN105073862B (zh) | 2022-02-08 |
AU2013277296A1 (en) | 2015-01-22 |
RU2633580C2 (ru) | 2017-10-13 |
EP3546508A1 (en) | 2019-10-02 |
MX2014015390A (es) | 2015-03-05 |
ES2740752T3 (es) | 2020-02-06 |
CN105073862A (zh) | 2015-11-18 |
EP3546508B1 (en) | 2022-12-28 |
EP2861655B1 (en) | 2019-05-08 |
EP2861655A4 (en) | 2016-03-23 |
WO2013192227A1 (en) | 2013-12-27 |
AU2013277296B2 (en) | 2016-08-11 |
CN114526577A (zh) | 2022-05-24 |
ES2936462T3 (es) | 2023-03-17 |
CA2876958A1 (en) | 2013-12-27 |
US20170146291A1 (en) | 2017-05-25 |
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