| 000 | 01767nmc a2200313 4500 | ||
|---|---|---|---|
| 005 | 20260608201318.0 | ||
| 008 | 260224s xxu ing | ||
| 041 | _aInglés | ||
| 100 | 1 |
_aHernandez-Valencia, Vicente N. _925823 |
|
| 100 | 1 |
_aHlavinka, Michael W. _925824 |
|
| 100 | 1 |
_aBullin, Jerry A. _925817 |
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| 110 | 2 |
_aBryan Research & Engineering _925815 |
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| 245 | 0 | 0 | _aDesign glycol units for maximum efficiency |
| 270 | _a2009-05-22 ; 18/12/2003 | ||
| 500 | _aArtículo publicado en la página web de Bryan Research & Engineering(http://www.bre.com) donde se pueden consultar otros artículos sobre temas relacionados. ; Página web visitada en enero de 2004. ; Navegadores de Internet | ||
| 520 | _aIn designing dehydration units for natural gas, several critical parameters exist which can be varied to achieve a specified dew point depression. This paper studies the effects of varying the glycol flow rate, number of stages in the contactor, reboiler temperature, and stripping gas rate on water content in glycol dehydration units. The effect of high carbon dioxide composition in the feed is also presented. Finally, the emissions of aromatic (BTEX) and other VOC's from the regenerator and flash will be considered. | ||
| 650 | 0 |
_aTratamiento de gas natural _9382 |
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| 650 | 0 |
_aTratamiento de gas con glicoles _95106 |
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| 650 | 0 |
_aDeshidratación _9278 |
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| 650 | 0 |
_aGlicoles _9279 |
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| 650 | 0 |
_aAlcoholes _97200 |
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| 650 | 0 |
_aHidratos en gas natural _91130 |
|
| 700 | 1 |
_aHlavinka, Michael W. _925824 |
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| 700 | 1 |
_aBullin, Jerry A. _925817 |
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| 710 | 2 |
_aBryan Research & Engineering _925815 |
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| 856 | _uhttp://www.bre.com/technicalpapers/technicalpaper.asp?articlenumber=34 | ||
| 942 | _cARCHIVO | ||
| 999 |
_c153274 _d153274 |
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