CARBON-MONOXIDE PRODUCTION FROM DEGRADATION OF DESFLURANE, ENFLURANE,ISOFLURANE, HALOTHANE, AND SEVOFLURANE BY SODA LIME AND BARALYME(R)

Citation
Zx. Fang et al., CARBON-MONOXIDE PRODUCTION FROM DEGRADATION OF DESFLURANE, ENFLURANE,ISOFLURANE, HALOTHANE, AND SEVOFLURANE BY SODA LIME AND BARALYME(R), Anesthesia and analgesia, 80(6), 1995, pp. 1187-1193
Citations number
13
Categorie Soggetti
Anesthesiology
Journal title
ISSN journal
00032999
Volume
80
Issue
6
Year of publication
1995
Pages
1187 - 1193
Database
ISI
SICI code
0003-2999(1995)80:6<1187:CPFDOD>2.0.ZU;2-J
Abstract
Anecdotal reports suggest that soda lime and Baralyme(R) brand absorbe nt can degrade inhaled anesthetics to carbon monoxide (GO). We examine d the factors that govern CO production and found that these include: 1) The anesthetic used: for a given minimum alveolar anesthetic concen tration (MAC)-multiple, the magnitude of CO production (greatest to le ast) is desflurane greater than or equal to enflurane > isoflurane >> halothane = sevoflurane. 2) The absorbent dryness: completely dry soda lime produces much more CO than absorbent with just 1.4% water conten t, and soda lime containing 4.8% or more water (standard soda lime con tains 15% water) generates no CO. In contrast, both completely dry Bar alyme(R) and Baralyme(R) with 1.6% water produce high concentrations o f CO, and Baralyme(R) containing 4.7% water produces concentrations eq ualing those produced by soda Lime containing 1.4% water. Baralyme(R) containing 9.7% or more water and standard Baralyme(R) (13% water) do not generate CO. 3) The type of absorbent: at a given water content, B aralyme(R) produces more CO than does soda lime. 4) The temperature: a n increased temperature increases CO production. 5) The anesthetic con centration: more CO is produced from higher anesthetic concentrations. These results suggest that CO generation can be avoided for all anest hetics by using soda lime with 4.8% (or more) water or Baralyme(R) wit h 9.7% (or more) water, and by using inflow rates of less than 2-3 L/m in. Such inflow rates are low enough to ensure that the absorbent does not dry out.