[••$31 B L U E M J
Where The Choice Is Yours OVER 1000 MODELS
OVENS
Blue M has anticipated your every oven need with a choice of over 1000 models . . . ranging from a $200 lab oven on up to a $20,000 fully automated inert gas chamber with microprocessing control. Mechanical and gravity . . . sizes to 96 cu. ft. . . . temperatures to +704°C. Batch . . . Life-Test . . . Utility . . . Burn-In . . . Drawer . . . High-Powered . . . Vacuum . . . Drying — even FRICTION-AIRE* the patented electric chambers with no heating elements. Most have Blue M control systems for superior performance - plus such other standard features as welded stainless interiors, elapsed time meters, overtemperature protection. It's easily America's finest, most complete line. Choice. With Blue M it does mean selection. And with Blue M, choice also means highest quality. We offer you both. Is anything less worth your time? Where the choice is yours: Blue M Electric Company; Corporate Head quarters; Blue Island, Illinois 60406; Telephone: (312) 385-9000.
e£ BLUE M CIRCLE 27 ON READER SERVICE CARD
INTRODUCING UNISEAL® PRESSURE MEASURING SYSTEM An innovation that counts UN1SE AL ' sets n e w standards ot accuracy and s i m p l i c i t y , upens up n e w h u n z o n s lor non invasive p r e s s u r e m e a s u r e m e n t s in c l o s e d s y s t e m s by external contact only " U N I S E A L » adds a vital d i m e n s i o n 10 your e x p e r i m e n t a l evaluations by obtaining absolute values of pressure w i t h Uniseal'5 Pressure Measuring System.
> HIGHLIGHTS :
• Se'f c o n t a i n e d c l o s e d s y s t e m simple s e a l i n g no leakage p r o b l e m s · Pressure values by e x t e r n a l surface contact only · No pressure St Π MM t U be i n s e r t e d into reactor . hence; no v o l u m e c h a n g e / no volume* corrections/ no c o n t a m i n a t i o n uf s p e c i m e n / no pressure se.isor lo damage · Reliable pressure data at t e m p é r a t u r e s up to 180° C • Ideal lor c o r r o s i v e s y s t e m s · S i m p l e to operate APPLICATIONS : Analytical chemistry Explosives • Energy calculations » Sitmplt? weigh ι optimization Organic Chemistry • Vapour pressure Studies by pressure determination • Bio applications • Critical pressures • Operational siitcty evaluation • Clinical applications • Chemical equilibrium • protem hydrolysis • Pressure characteristics υΐ studies • Carnoiiyl complexes unknown samples • Oxidation • reduction • Organo-meiallic compounds Chemical Engineering equilibria • Polymerization studies Inorganic Chemistry • Solubility studies • Ceramics Physical and Theoretical • Solubility products and Chemistry • Fertilizers precipitation • Reaction kinetics • Geochemistry Propel lantt • Caseous reactions - rate • Glasses studies • Metallurgy • Noble gas reactions • Refractories
*..-.·.---.·..
UNISEAL DECOMPOSITION VESSELS LTD. PO.Bux lJ
t
HAIFA jloy4 ISRAEL · Tel 04-244990 · ΓβΙβχ Available in USA and Canada from
BXHA M. 4f>400 EXI 8610
COLUMBIA ORGANIC CHEMICALS CO., INC. Ρ Ο Box 9096.
Columbia. S C 29290.
Phone
(803)770 4990
CIRCLE 210 ON READER SERVICE CARD
950 A • ANALYTICAL CHEMISTRY, VOL. 53, NO. 8, JULY 1981
5
separative performance, hinging on thoughtful experimental design. The equations also show the magnitude of potential gains stemming from the stretching of limiting operating pa rameters, such as pressure or voltage. Furthermore, the equations show where little progress is to be expected, thus helping close off unproductive pathways. Table II shows performance ceilings for a group of contrasting techniques. Equations are shown for both separat ing power and speed. Separating power is expressed in terms of number of theoretical plates Ν (applicable even to electrophoresis (9)), and in terms of peak capacity n, the latter more generally useful because the plate concept does not extend well to such steady-state methods as isoelec tric focusing (10). Ceilings for separation speed are ex pressed as number of plates per unit time, N/t. Table II has, of course, been simpli fied in the interest of clarity, and does not begin to explain how each equa tion is to be used or the nature of any qualifications. But it captures the es sence if not the details of each meth od's potential. The equations have been collected from the previously cited literature (5, 7-11). Even casual inspection shows that there are many similarities among the equations in any of the columns of Table II. This reflects the underlying systematics of separation, but space permits only a few points in this regard. We note that the terms θ and Θ' rep resent the extent to which any disper sive process increases zone spreading. Ideally, θ at 0* at 1. Parameter y plays the same role in the chromatographic equations, but is usually less than unity due to tortuous diffusion in packed columns. Ν is always inversely proportional to one of these parame ters, while η is always inversely pro portional to the square root of one of them. Reducing θ or Θ' is therefore a general goal for separations. Of significance, we note that every equation for separation speed N/t is inversely proportional to friction coef ficient /, or proportional to diffusivity D, which is one and the same thing ac cording to Equation 3. This illustrates the validity of our earlier general con clusion that separation time is scaled with / and separation speed inversely with / and directly with D. (No sepa ration speed equations are available for the steady-state methods where zones form by an unusual mechanism
(ID). We note also that peak capacities are almost the same in the two com plementary pairs: electrophoresis-iso electric focusing and rate zonal sedimentation-isopyenic sedimentation