WO2005116166A1 - Procede permettant de separer la cire de materiaux siliceux - Google Patents
Procede permettant de separer la cire de materiaux siliceux Download PDFInfo
- Publication number
- WO2005116166A1 WO2005116166A1 PCT/IB2005/051742 IB2005051742W WO2005116166A1 WO 2005116166 A1 WO2005116166 A1 WO 2005116166A1 IB 2005051742 W IB2005051742 W IB 2005051742W WO 2005116166 A1 WO2005116166 A1 WO 2005116166A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- wax
- oil
- mixture
- weight
- product
- Prior art date
- Legal status (The legal status 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 status listed.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/04—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
Definitions
- the present invention relates to a process for material preparation.
- the present invention relates to a process for material preparation for preparing a natural wax composition.
- Wax includes esters of monohydric alcohols of the higher homologues; e.g. beeswax is the myricyl (melissyl) ester of palmitic acid.
- Oils are a group of neutral lipids that are liquid at room temperature.
- Fixed (fatty) oils from animal, vegetable and marine sources, consist chiefly of glycerides and esters of fatty acids, and also include essential oils (volatile products, mainly hydrocarbons, with characteristics odours, derived from certain plants).
- Mineral oils, derived from petroleum, coal, shale, etc. consist of hydrocarbons. Waxes and oils are used inter alia in the cosmetic industry.
- a process for material preparation includes the step of separating wax and/or organics and/or oil from used siliceous material.
- a material preparation apparatus for separating wax and/or oil from used siliceous material includes separating means for separating wax and/or organics and/or oil from used siliceous material to obtain wax and/or organics and/or oil.
- the process may be used to recycle used siliceous material.
- the used siliceous material may include perlite.
- the used siliceous material may include diatomaceous earth.
- the oil may be vegetable oil.
- the unused siliceous material such as unused refined siliceous material may be added to the used siliceous material.
- the process may include the step of mixing the used siliceous material including the wax and/or organics and/or oil, with water to obtain a first mixture.
- the first mixture may be subjected to heat up to 100 degrees Celcius.
- the heat may be provided via steam and/or boilers.
- the first mixture may be heated for 2-3 hours.
- the wax and/or oil may form the top layer of the first mixture and the perlite and water the bottom layer of the mixture due to phase separation and left overnight to settle.
- the wax and/or oil mixture may be pumped off.
- the perlite and water mixture may have the following composition :
- the wax/oil mixture may be pumped into retaining tanks.
- Oil and wax settlement may take place over a period of 30 to 60 days.
- the wax may settle at the bottom as a grey wax mixture.
- the oil may settle at the top.
- the oil may be pumped off on a weekly basis.
- a grey wax mixture may be obtained including about 40 weight % oil and 2 weight % organic matter.
- the grey wax mixture may be subjected to boiling.
- the boiling may take place in a cooking tank having coils.
- the boiled wax mixture may be passed through a 200-300 micron filtration system at a temperature of 100 degrees Celcius to obtain a wax filtrate product.
- the wax filtrate product may have the following composition :
- the wax filtrate product may include no organic matter due to the filtration.
- the wax filtrate product may be used in the cosmetic industry as a basis, for lipsticks, eyeliners, base creams and other body and facial lather applications.
- the wax filtrate product may be used in the fruit industry for coating of fruits.
- the wax filtrate product may be used in the pharmaceutical industry in the coating of capsules.
- the wax filtrate product may be a natural product.
- the invention also extends to any product obtained by means of the aforesaid process.
- Tablel typical physical characteristics of raw perlite
- Table 5 chemical analysis of wax filtrate product
- Table 6 protein composition of wax filtrate product and carbon structure single and double bond compositions.
- One embodiment of a process for material preparation in accordance with the invention includes the step of separating wax and/or oil from used siliceous material which generally includes perlite and is unused refined siliceous material.
- the process includes the steps
- the perlite and water mixture has the following composition : (a) Perlite 58 weight %
- the grey wax/oil/organic mixture Before separation, the grey wax/oil/organic mixture has a composition of about 40 weight % oil and 2 weight % organic matter.
- the wax filtrate product has the following composition :
- the wax filtrate product includes no organic matter due to the filtration.
- the wax filtrate product once developed to specification can be used in the cosmetic industry as a basis, for lipsticks, and eyeliners.
- the wax filtrate product can be used in the fruit industry for coating of fruits.
- the wax filtrate product can be used in the pharmaceutical industry in the coating of capsules.
- the wax filtrate product is a natural product as no chemicals are added during the process.
- Table 1 provides the typical physical characteristics of raw perlite
- Table 2 provides the typical chemical analysis of raw perlite
- Table 3 provides the physical characteristics of treated perlite
- Table 4 provides the chemical analysis of treated perlite
- Table 5 provides the chemical analysis of the wax filtrate product
- Table 6 provides protein composition of wax filtrate product.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Medicinal Preparation (AREA)
- Cosmetics (AREA)
- Fats And Perfumes (AREA)
Abstract
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ZA2004/1620 | 2004-05-27 | ||
| ZA200401620 | 2004-05-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2005116166A1 true WO2005116166A1 (fr) | 2005-12-08 |
Family
ID=35450879
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/IB2005/051742 Ceased WO2005116166A1 (fr) | 2004-05-27 | 2005-05-27 | Procede permettant de separer la cire de materiaux siliceux |
Country Status (2)
| Country | Link |
|---|---|
| WO (1) | WO2005116166A1 (fr) |
| ZA (1) | ZA200609045B (fr) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4415432A (en) * | 1980-11-19 | 1983-11-15 | Standard Oil Company (Indiana) | Hydrocarbon recovery method and apparatus |
| US4448669A (en) * | 1983-03-16 | 1984-05-15 | Phillips Petroleum Company | Hydrocarbon recovery from diatomite |
| DE3323770A1 (de) * | 1983-07-01 | 1985-01-03 | Metallgesellschaft Ag, 6000 Frankfurt | Verfahren zum trocknen und erhitzen von oelhaltigen feststoffen |
| US4495058A (en) * | 1983-06-06 | 1985-01-22 | Chevron Research Company | Process for generating superheated steam using retorted solids |
| US4539093A (en) * | 1982-12-16 | 1985-09-03 | Getty Oil Company | Extraction process and apparatus for hydrocarbon containing ores |
| CA1196594A (fr) * | 1982-04-08 | 1985-11-12 | Guy Savard | Extraction du petrole present dans les sables bitumineux |
| US4571294A (en) * | 1984-07-02 | 1986-02-18 | Getty Oil Company | Process for extracting hydrocarbons from hydrocarbon bearing ores |
| WO2004101461A1 (fr) * | 2003-05-19 | 2004-11-25 | Francois Jacques Labuschagne | Procede de traitement de materiau |
-
2005
- 2005-05-27 WO PCT/IB2005/051742 patent/WO2005116166A1/fr not_active Ceased
-
2006
- 2006-10-31 ZA ZA200609045A patent/ZA200609045B/xx unknown
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4415432A (en) * | 1980-11-19 | 1983-11-15 | Standard Oil Company (Indiana) | Hydrocarbon recovery method and apparatus |
| CA1196594A (fr) * | 1982-04-08 | 1985-11-12 | Guy Savard | Extraction du petrole present dans les sables bitumineux |
| US4539093A (en) * | 1982-12-16 | 1985-09-03 | Getty Oil Company | Extraction process and apparatus for hydrocarbon containing ores |
| US4448669A (en) * | 1983-03-16 | 1984-05-15 | Phillips Petroleum Company | Hydrocarbon recovery from diatomite |
| US4495058A (en) * | 1983-06-06 | 1985-01-22 | Chevron Research Company | Process for generating superheated steam using retorted solids |
| DE3323770A1 (de) * | 1983-07-01 | 1985-01-03 | Metallgesellschaft Ag, 6000 Frankfurt | Verfahren zum trocknen und erhitzen von oelhaltigen feststoffen |
| US4571294A (en) * | 1984-07-02 | 1986-02-18 | Getty Oil Company | Process for extracting hydrocarbons from hydrocarbon bearing ores |
| WO2004101461A1 (fr) * | 2003-05-19 | 2004-11-25 | Francois Jacques Labuschagne | Procede de traitement de materiau |
Non-Patent Citations (1)
| Title |
|---|
| DATABASE WPI Week 198525, Derwent World Patents Index; Class Q76, AN 1985-007340 * |
Also Published As
| Publication number | Publication date |
|---|---|
| ZA200609045B (en) | 2008-04-30 |
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