[Characteristics of plasmid pBS271 controlling epsilon-caprolactam degradation by bacteria in the genus Pseudomonas]

Conjugative plasmids control the ability of five Pseudomonas strains isolated from the rectifiers of chemical plants to grow on epsilon-caprolactam as a sole carbon and nitrogen source. All the plasmids have a high molecular mass of their DNA (ca. 300 MDa) and control epsilon-caprolactam degradation at least to succinate. One of the plasmids (pBS271) belongs to the incompatibility group P-2 and suppresses the growth of a broad spectrum of temperate and virulent P. aeruginosa bacteriophages as well as that of some P. putida bacteriophages.

Erythrocyte arginase activity as an indicator of lead exposure

ABSTRACT A semi-automated method has been developed for the determination of the arginase activity of erythrocytes using dried blood spots, which are easy to prepare on site in a factory for later laboratory analysis. The mean arginase activity of erythrocytes in 49 men occupationally exposed to lead was 62·9 IU/g·Hb (SD, 14·4 IU/g·Hb); in 45 men not exposed to lead the mean was 44·6 IU/g·Hb (SD, 11·6 IU/g·Hb). A significantly higher mean arginase activity was found in the specimens from lead-exposed workers (p < 0·001). The correlation coefficient between blood lead and erythrocyte arginase was r = 0·67 (p < 0·001). The degree of correlation between blood lead and lead indicators including arginase was r = 0·75 for urine δ-aminolaevulinic acid, r = 0·67 for erythrocyte arginase, r = 0·66 for urine lead, and r = 0·63 for coproporphyrin. Erythrocyte arginase showed no significant correlation in the liver function tests, GOT, GPT, and albumin in serum. When 40 μg/100 g of blood lead concentration was fixed as the basic value and 56·2 IU/g·Hb of erythrocyte arginase activity was set as the screening value in lead-exposed workers, the sensitivity and specificity of the arginase test were 0·96 and 0·65, respectively. Thus the validity of the test was calculated to be 1·61. These results show that the arginase level of erythrocytes can be considered to be one of the significant indicators of occupational exposure to lead because it reflects well the dose-response relationship of lead in the human body. Our method allows rapid analysis of erythrocyte arginase and thus should be useful in screening for lead exposure.

Effect of alcohol on the kinetics of mandelic acid excretion in volunteers exposed to styrene vapour

The effect of a dose of alcohol on the kinetics of mandelic acid excretion in four volunteers exposed to 220 mg/m3 styrene has been investigated under controlled exposure chamber conditions. Ethanol inhibited the excretion of mandelic acid, so that the peak excretion was delayed from the end of the exposure period until three hours afterwards. One hour after administration of ethanol blood mandelic acid concentrations were 56% of the levels found during the alcohol-free control exposure, and this was paralleled by a 15-fold rise in phenylethane 1,2 diol, the metabolic precursor of mandelic acid. It is suggested that the inhibition of the oxidation of this diol is related to the change in NAD +/NADH ratio produced by ethanol metabolism. The implications of this ethanol effect on the interpretation of urinary mandelic acid excretion when monitoring workers exposed to styrene are discussed.

Occurrence of lung cancer in workers producing chromium pigments

The results of a follow-up study on the incidence of lung cancer in 133 workers producing zinc chromate pigments are presented. By the end of 1972 three cases of lung cancer had occurred in a sub-cohort of 24 workers who had been employed for over three years. The same group of workers has now been followed up to December 1980 and three further cases of lung cancer were found. The observed/expected ratio was 44 in this group, virtually the same as at the end of 1972. Five of the six patients smoked. Only one had been exposed to chromates other than zinc chromates.

[Concepts for the synthesis of new biologically active substances]

Three concepts for the synthesis of biologically active compounds are discussed and illustrated by examples. In addition to the accidental finding of biologically active compounds, synthesized purely for chemical reasons, analogy models can serve as guidelines for synthesis. In the latter, naturally occurring or synthetic biologically active molecules are modified to optimize or alter the biological properties. A third approach for the synthesis of active substances is oriented according to the side of action. Models from biochemistry and molecular biology serve as a basis for synthesis planning.

Chemical engineering in medicine in North America

An examination has been made of the involvement of chemical engineers in medicine in North America. Fields of Study and subjects of research are briefly given in tabular form and the general statistical picture of chemical engineering in medicine discussed. Further details of the workers and references to their published work can be obtained from the author if required.

Engineering analysis of continuous production of L-aspartic acid by immobilized Escherichia coli cells in fixed beds

The reaction mechanism and decay behavior of aspartase activity for immobilized Escherichia coli cells were investigated by using a sectional packed column. Reaction within the immobilized cell column proceeded at zero-order on substrate solutions ranging in concentration from 0.1 to 1.0M, and the initial reaction rate was found to be 1.556 X 10(-2) mol/min/liter of immobilized cells. The effect of temperature on the reaction rate constant was investigated. The Arrhenius plot was a straight line at temperatures below 43 degrees C, and the activation energy for immobilized cells was calculated to be 12.36 kcal/mol. Aspartase activity in the immobilized cell column decayed exponentially and uniformly in all sections of a column. Its half-life was approximately 120 days. The rate of formation of L-aspartic acid was shown to be independent of column dimensions.

Design methods for tubular fermentation systems

Methods for the design of tubular fermentation systems are summarized. The first part, on tubular system hydrodynamics, is concerned with the design methods for gas hold-up, pressure drop, drop-size distribution and actual interfacial area, and with non-ideal flow conditions. This being a critical review, only the more important methods have been selected. More recent design methods for the prediction of oxygen transfer coefficients in fermentation systems and methods of determining of true kinetic relations are also reviewed, accounting for the inevitable non-ideality of flow. General rules for system optimization are presented.