BR0006748A - Unidade modular de enriquecimento por difusão gasosa e fábrica de enriquecimento por difusão gasosa - Google Patents
Unidade modular de enriquecimento por difusão gasosa e fábrica de enriquecimento por difusão gasosaInfo
- Publication number
- BR0006748A BR0006748A BR0006748-2A BR0006748A BR0006748A BR 0006748 A BR0006748 A BR 0006748A BR 0006748 A BR0006748 A BR 0006748A BR 0006748 A BR0006748 A BR 0006748A
- Authority
- BR
- Brazil
- Prior art keywords
- enrichment
- unit
- gas diffusion
- modular
- diffused
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D59/00—Separation of different isotopes of the same chemical element
- B01D59/10—Separation by diffusion
- B01D59/12—Separation by diffusion by diffusion through barriers
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
"UNIDADE MODULAR DE ENRIQUECIMENTO POR DIFUSãO GASOSA E FáBRICA DE ENRIQUECIMENTO POR DIFUSãO GASOSA". Compreendendo uma unidade de enriquecimento por difusão gasosa, do tipo de cascata de enriquecimento, sendo um módulo integrado, que contém todos os elementos da unidade, com vários fluxos de circulação com diferente grau de enriquecimento, compreendendo um compressor axial em trabalho simultâneo de compreensão de ditos fluxos, um difusor com membranas. O fluído difundido (enriquecido) passa ao compressor em outra seção para realizar a seguinte etapa de enriquecimento e a saída de fluxo não difundido conecta-se a um injetor para nivelar as pressões e reciclar o material empobrecido. A referida unidade modular de enriquecimento isotópico integra múltiplas etapas de enriquecimento para conseguir um alto rendimento separativo mediante a recirculação interna de uma fração do fluído difundido de cada etapa. O compressor axial multifluxo é acionado por uma turbina de gás e os gases de saída da turbina e o calor gerado no processo são injetados em um ciclo térmico. No centro da unidade existe uma sonda para efetuar análise não destrutiva. A fábrica de enriquecimento por difusão gasosa, compreende ditas unidades modulares de enriquecimento conectadas em série e os números de etapas de 1 ou mais de ditas unidades é diferente. Uma aplicação da presente invenção é sua utilização para a separação isotópica do hexafluoreto de urânio em fase gasosa.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR0006748-2A BR0006748A (pt) | 2000-11-29 | 2000-11-29 | Unidade modular de enriquecimento por difusão gasosa e fábrica de enriquecimento por difusão gasosa |
AU2002210287A AU2002210287A1 (en) | 2000-11-29 | 2001-10-17 | Gaseous diffusion enrichment modular unit and gaseous diffusion enrichment plant |
PCT/BR2001/000131 WO2002043836A1 (en) | 2000-11-29 | 2001-11-16 | Gaseous diffusion enrichment modular unit and gaseous diffusion enrichment plant |
US10/447,555 US20040060441A1 (en) | 2000-11-29 | 2003-05-29 | Gaseous diffusion enrichment modular unit |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR0006748-2A BR0006748A (pt) | 2000-11-29 | 2000-11-29 | Unidade modular de enriquecimento por difusão gasosa e fábrica de enriquecimento por difusão gasosa |
Publications (1)
Publication Number | Publication Date |
---|---|
BR0006748A true BR0006748A (pt) | 2005-08-09 |
Family
ID=3946275
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR0006748-2A BR0006748A (pt) | 2000-11-29 | 2000-11-29 | Unidade modular de enriquecimento por difusão gasosa e fábrica de enriquecimento por difusão gasosa |
Country Status (4)
Country | Link |
---|---|
US (1) | US20040060441A1 (pt) |
AU (1) | AU2002210287A1 (pt) |
BR (1) | BR0006748A (pt) |
WO (1) | WO2002043836A1 (pt) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102824808B (zh) * | 2012-08-21 | 2014-05-28 | 西安交通大学 | 一种利用太阳能富集煤矿瓦斯的系统 |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB860752A (en) * | 1943-01-20 | 1961-02-08 | Atomic Energy Authority Uk | Improvements in or relating to the separation of gaseous and vaporous media |
US3208197A (en) * | 1944-11-03 | 1965-09-28 | Simon Franz Eugen | Diffusion separation of fluids |
US4104037A (en) * | 1957-09-23 | 1978-08-01 | The United States Of America As Represented By The United States Department Of Energy | Gaseous diffusion system |
US3274750A (en) * | 1962-12-28 | 1966-09-27 | Gen Electric | Permeable polymeric membrane gas separation |
US3996470A (en) * | 1974-10-15 | 1976-12-07 | Jersey Nuclear-Avco Isotopes, Inc. | Laser alteration of accommodation coefficient for isotope separation |
US4040801A (en) * | 1976-04-05 | 1977-08-09 | The United States Of America As Represented By The United States Energy Research And Development Administration | Method and apparatus for rapid adjustment of process gas inventory in gaseous diffusion cascades |
FR2388591A1 (fr) * | 1977-04-29 | 1978-11-24 | Commissariat Energie Atomique | Assemblage de contacteurs-separateurs dans une installation d'extraction |
WO1980000010A1 (en) * | 1978-06-05 | 1980-01-10 | R Schlenker | Method for separating isotopes |
JPS585688B2 (ja) * | 1979-03-09 | 1983-02-01 | 若尾 法昭 | クヌッセン細孔拡散膜の移動式ガス混合物成分濃縮装置 |
DE2947089A1 (de) * | 1979-11-22 | 1981-05-27 | Helmut Dr.-Ing. 5804 Herdecke Michele | Verfahren zur trennung von fluiden durch permeation |
NZ196665A (en) * | 1980-04-21 | 1983-07-15 | Atomic Energy Board | Separation of gases by cascade process |
US4424067A (en) * | 1982-07-29 | 1984-01-03 | Allied Corporation | Purification of anhydrous hydrogen fluoride |
GB8830107D0 (en) * | 1988-12-23 | 1989-02-22 | Boc Group Plc | Gas separation |
US5378263A (en) * | 1992-12-21 | 1995-01-03 | Praxair Technology, Inc. | High purity membrane nitrogen |
US6280626B1 (en) * | 1998-08-12 | 2001-08-28 | Mitsubishi Rayon Co., Ltd. | Membrane separator assembly and method of cleaning the assembly utilizing gas diffuser underneath the assembly |
NO308401B1 (no) * | 1998-12-04 | 2000-09-11 | Norsk Hydro As | FremgangsmÕte for gjenvinning av CO2 som genereres i en forbrenningsprosess samt anvendelse derav |
FR2802114B1 (fr) * | 1999-12-09 | 2002-06-28 | Air Liquide | Installation et procede de separation de gaz par permeation selective |
US6273937B1 (en) * | 2000-03-29 | 2001-08-14 | Trans Ionics Corporation | Membrane pervaporation and vapor permeation system |
EP1299172A4 (en) * | 2000-05-17 | 2006-04-05 | Bechtel Bwxt Idaho Llc | METHOD AND APPARATUS FOR REMOVING NON-CONDENSABLE GAS FROM A WORKING FLUID IN A BINARY GENERATING SYSTEM |
-
2000
- 2000-11-29 BR BR0006748-2A patent/BR0006748A/pt not_active Application Discontinuation
-
2001
- 2001-10-17 AU AU2002210287A patent/AU2002210287A1/en not_active Abandoned
- 2001-11-16 WO PCT/BR2001/000131 patent/WO2002043836A1/en not_active Application Discontinuation
-
2003
- 2003-05-29 US US10/447,555 patent/US20040060441A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
AU2002210287A1 (en) | 2002-06-11 |
WO2002043836A1 (en) | 2002-06-06 |
US20040060441A1 (en) | 2004-04-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
B25C | Requirement related to requested transfer of rights | ||
B25B | Requested transfer of rights rejected | ||
B03A | Publication of a patent application or of a certificate of addition of invention [chapter 3.1 patent gazette] | ||
B11A | Dismissal acc. art.33 of ipl - examination not requested within 36 months of filing | ||
B11Y | Definitive dismissal - extension of time limit for request of examination expired [chapter 11.1.1 patent gazette] |