MD3362F1 - Plant for flow production of fatty acid esters - Google Patents
Plant for flow production of fatty acid esters Download PDFInfo
- Publication number
- MD3362F1 MD3362F1 MDA20070030A MD20070030A MD3362F1 MD 3362 F1 MD3362 F1 MD 3362F1 MD A20070030 A MDA20070030 A MD A20070030A MD 20070030 A MD20070030 A MD 20070030A MD 3362 F1 MD3362 F1 MD 3362F1
- Authority
- MD
- Moldova
- Prior art keywords
- reactor
- tanks
- tank
- fatty acid
- outlet
- Prior art date
Links
- 235000014113 dietary fatty acids Nutrition 0.000 title abstract 3
- 229930195729 fatty acid Natural products 0.000 title abstract 3
- 239000000194 fatty acid Substances 0.000 title abstract 3
- -1 fatty acid esters Chemical class 0.000 title abstract 3
- 238000004519 manufacturing process Methods 0.000 title abstract 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract 3
- 150000002148 esters Chemical class 0.000 abstract 2
- 238000005809 transesterification reaction Methods 0.000 abstract 2
- 238000010908 decantation Methods 0.000 abstract 1
- 235000013305 food Nutrition 0.000 abstract 1
- 239000003921 oil Substances 0.000 abstract 1
- 235000019198 oils Nutrition 0.000 abstract 1
- 230000002093 peripheral effect Effects 0.000 abstract 1
- 239000011541 reaction mixture Substances 0.000 abstract 1
- 125000006850 spacer group Chemical group 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 235000015112 vegetable and seed oil Nutrition 0.000 abstract 1
- 239000008158 vegetable oil Substances 0.000 abstract 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Fats And Perfumes (AREA)
Abstract
Inventia se refera la utilajele pentru producereain flux a esterilor acizilor grasi din uleiuri vegetale si poate fi utilizata in industriile chimica, alimentara si de prelucrare. nstalatia de producere in flux a esterilor acizilor grasi include uncorp cilindric divizat in trei rezervoare coaxiale (1, 2, 3) cu fund comun. Rezervoarele central (3) si periferic (1) fiind predestinate pentru receptia si decantarea amestecului de reactie obtinut respectiv dupa prima si a doua treapta de transesterificare. Rezervoarele (1, 3) sunt dotate cu dispozitive de receptie (10, 11) si de evacuare (5, 6) a esterilor obtinuti si racorduri de evacuare aglicerinei. Intre rezervoarele (1, 3) este situatrezervorul schimbatorului de caldura (2), in caresunt amplasate reactoarele primei si, respectiv,a celei de a doua treapta de transesterificare (12, 13). Reactoarele (12, 13) sunt formate din mai multe tuburi unite consecutiv. In fiecare tub fiind instalate rondele centrifuge, fixate perpendicular fata de axa tubului cu ajutorul unor bucse de distantare. Capetele tuburilor sunt inchise cu flanse, in care sunt executate orificii filetate, prin intermediul carora ele se unesc cu urmatorul tub. Racordul de debitare a uleiului si metanolului este unit cu un ejector (38) si o pompa de inalta presiune (14). Iesirea pompei (14) este unita cu reactorul (12). Iesirea din reactorul (12) este unita cu dispozitivul de receptie (10) al rezervoruluicentral (3). Dispozitivul de evacuare a esterilor(6) din rezervorul (3) este unit cu reactorul (13) prin intermediul ejectorului (9) si a unei pompede inalta presiune (17). Iesirea din reactorul (13) este unita cu dispozitivul de receptie (11) al rezervorului (1).The invention relates to machines for the flow production of fatty acid esters from vegetable oils and can be used in the chemical, food and processing industries. The fatty acid ester production plant includes a cylindrical body divided into three coaxial tanks (1, 2, 3) with a common bottom. The central (3) and peripheral (1) tanks being predestined for the reception and decantation of the reaction mixture obtained respectively after the first and second transesterification stage. The tanks (1, 3) are equipped with devices for receiving (10, 11) and evacuating (5, 6) the obtained esters and agglerinin discharge connections. Between the tanks (1, 3) is located the heat exchanger tank (2), in which are located the reactors of the first and, respectively, of the second transesterification stage (12, 13). The reactors (12, 13) consist of several tubes connected in a row. Centrifugal washers are installed in each tube, fixed perpendicular to the axis of the tube with the help of spacer bushes. The ends of the tubes are closed with flanges, in which threaded holes are made, through which they are connected to the next tube. The oil and methanol flow connection is connected to an ejector (38) and a high pressure pump (14). The pump outlet (14) is connected to the reactor (12). The outlet of the reactor (12) is connected to the receiving device (10) of the central tank (3). The ester discharge device (6) from the tank (3) is connected to the reactor (13) by means of the ejector (9) and a high pressure pump (17). The outlet of the reactor (13) is connected to the receiving device (11) of the tank (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| MDA20070030A MD3362G2 (en) | 2007-02-02 | 2007-02-02 | Plant for flow production of fatty acid esters |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| MDA20070030A MD3362G2 (en) | 2007-02-02 | 2007-02-02 | Plant for flow production of fatty acid esters |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| MD3362F1 true MD3362F1 (en) | 2007-07-31 |
| MD3362G2 MD3362G2 (en) | 2008-02-29 |
Family
ID=38331523
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MDA20070030A MD3362G2 (en) | 2007-02-02 | 2007-02-02 | Plant for flow production of fatty acid esters |
Country Status (1)
| Country | Link |
|---|---|
| MD (1) | MD3362G2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| MD3650G2 (en) * | 2007-07-16 | 2009-02-28 | Институт Сельскохозяйственной Техники "Mecagro" | Installation for two-stage transesterification of fat acids |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PT1034160E (en) * | 1997-11-24 | 2002-10-31 | Energea Umwelttechnologie Gmbh | METHOD FOR THE PRODUCTION OF FATTY ACID METHYL ESTER AND EQUIPMENT FOR PERFORMING THE SAME |
| MD2830G2 (en) * | 2004-01-14 | 2006-03-31 | Зайфулла Хамит-Нагимо0 СУЛЕЙМАНОВ | Installation for obtaining fatty acids of the methyl esters |
| MD2958C2 (en) * | 2004-04-22 | 2006-11-30 | Валериу ДОМИНАС | Installation for obtaining biodiesel fuel from vegetal oils |
-
2007
- 2007-02-02 MD MDA20070030A patent/MD3362G2/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| MD3362G2 (en) | 2008-02-29 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG4A | Patent for invention issued | ||
| KA4A | Patent for invention lapsed due to non-payment of fees (with right of restoration) | ||
| MM4A | Patent for invention definitely lapsed due to non-payment of fees |