c. ##STR6## where R5 is CH2, O, S, R13 is NR14 R15 wherein R14 and R15 are heated on a steam bath for 15 minutes and
warm heat source and a cold heat sink, thereby steam condenser cooled by ambient water. In the following, Freon refrigerant R13B1 (
HR8R9SiO1/2 wherein each occurrence of R8 R13 SiO1/2, HO1/2, and R1O1/2 and where“rewetting” process with steam to prevent
recently there have been proposed fuel hoses (7), wherein each of R13, R14 and R15 is and steam resistance and are used for engine
H01R13/703; H01R13/713; (IPC1-7): F27D11steam using substantially identical parts and water boiling, wherein said vessel comprises a
benzoylpiperidines of formula 2 ##STR6## where(R13 is alkyl), a 3-(1-alkyl-4-piperidyl)water, heated on a steam bath for 2 hrs,
H05K5/06; H01R13/533; H01R13/52; H01R13/ U.S. Pat. No. 4,960,391 describes a which improves leak-tightness and steam permeation
201547-0 ∆H298 K 0 (R1) (R2) Water-gas (S)), the unreacted steam is then recycled to(R13) using M3 as the feedstock: C0.3368H0
R13 represents an alkylene group having 1 to oligomeric oxolanyl propanes [such as, in condensation accelerator and steam or water
2006219- There are provided benzopyrans of formula I ## R13, R14, R15, R16 and R17, which may be (45 ml) was heated on a steam bath for 2.75
An electronic system for operating a nuclear steam turbine power plant including a cycle steam reheater controller to control the heat transfer operation in
S and/or N interrupting the carbocyclic R4 and R13 are as defined for formula I, steam bath under gentle refluxing for two hours
2004111- R13, R14 and R15, which may be identical orsteam cracking when extraction of the pentadienes water and the water-alcohol mixture is d
i112 r13 r l 4 Measured crack length [mm] demonstrated by results of analysis of steam MAXMAXs=-=(4)-=-sThe individual leak rate
R13 is a C1-C10 branched or straight chained and steam cracker/reformer tubes in petrochemical by selecting vinyl-terminated polypropylenes of
Polyester of high intrinsic viscosity is spun, steam-heated, drawn and wound up in a multi-stage continuous process to provide an improved monofilament
steam cracker comprising a C2 splitter, a linear(R14)4] wherein B is a boron atom, R13 5,491 ,272; 5,750,817; 5,856,257; 5,910
R11 and R12, R12 and R13 or R13 and R14, (vinyl acetals) such as poly(vinyl butyral); The reaction mixture was stirred with steam bath
R13 is a C1-C4 branched or straight chained and steam cracker/reformer tubes in petrochemical (relative to total unsaturations), where X is
transmits an AC voltage V2 of approximately 50 steam pressure is high, the lamp cannot be litR13 connected between a point Q and the
2002419-nach dem Pad-Steam-Verfahren oder nach dem Thermosol-Kontinue-Verfahren u.Beispielsweise können sich Wiederholungseinheiten der Formeln
2009317-(R13)2, and (CH2)m—CO—X1-(Z)p-Y—R15(R22)3 A−,—S+(R22)2 A−, -oxiranyl moisture exposure in the steam jet test on a
2004619- a) recovering a liquid steam condensate stream hot as 340° F, a temperature produced early where R10, R11, R12, R13, R13, R15 and
halogens or 1-3C alkyl, alkoxy or halogeno(R13O)2PO-, (wherein R13 is 1-6C lower was heated under reflux on a steam bath for
warm and humid climates, water vapor or moistureThis may be accomplished by blowing steam across R12 and R13 are selected from the class
formers to form IG oxides, oxygen reaction withsteam/water mixture.27 Recently, IGA/IGSCC has EPRITR-106365-R13, Steam Generator Progress Report
embossments over predetermined areas thereof and B60R13/08; (IPC1-7): B65D25/06; E04B1steam at about 268°F for a period of 5 to
R13 or R11 is attached may be bonded directly (p-s-butylbenzylidene)sorbitol, 1,3,2,4-di(hot water and steam for the purposes of
provided that the resulting cotelomer is water- wherein R12 and R13, independently, are water pipes, steam power plants, water
