PB 1Q8 810
APPLICABILITY OF CATALYTIC OXIDATION TO THE DEVELOPMENT OF
NEW PROCESSES FOR REMOVING S02 FROM FLUE GASES. VOLUME III.
INDEXED BIBLIOGRAPHY
R. E. Opferkuck, et al
Monsanta Research Corporation
Dayton, Ohio
Aueust 1970
NATIONAL "ECHNiCAL INFORMATION SERVICE
Distributed . , ,'to foster, serve and promote the
nation's economic development
and technological advancement.'
U.S. DEPARTMENT OF COMMERCE
This document has been approved for public release and sale.
-------
3$ffiB£$:;*M
TtiTHE
FOR REMOVING S02 FROM RUE GASES
r i • > ' - ' •
INDEXED BI
S.M Mehta
A.H. Kon*t»m
OJ_ Zander*
H.R.'Strep
- Fncm CmM ******
Air P»U.ti«
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• •
•
NATIONAL TECHNICAL
INFORMATION SERVICE
MRC-DA-2U5
APPLICABILITY OP CATALYTIC OXIDATION TO
THE DEVELOPMENT OF NEW PROCESSES FOR
REMOVING SO2 PROM FLUE GASES
Volume III - Indexed Bibliography
Contract No. PH 22-68-12
MRC Job No. 6708
Prepared by
R. E. Opferkuch, Project Leader
S. M. Mehta
A. H. Konstam
D. L. Zanders
H. R. Strop
MONSANTO RESEARCH CORPORATION
DAYTON LABORATORY
Dayton, Ohio 15407
August 1970
Submitted to
Process Control Engineering Program
National Air Pollution Control Administration
Environmental Health Service
U. S. Department of Health, Education, and Welfare
5710 Wooster Pike
Cincinnati, Ohio 15277
-------
FOREWORD
PROJECT GENERAL SUMMARY
The intent of this volume Is to provide quick and convenient ac-
cess to all Information accumulated during the literature search
phase of the project. The actual listing of Information was
accomplished with the utilization of a computer, therefore the
page format is somewhat different than the previous two volumes.
Each section has an index tab for quick access.
This final report is presented In three volumes in an effort to
make the material accessible on the assumption that it is of
practical value and therefore will be put to use.
Volume I is Intended to contain all, and only, that material de-
rived from, or related to, the literature search. Essentially
all information in Volume I Is directly based on the literature.
Volume II. presents data and information generated in the labora-
tory and.on the drawing board. •
Volume III Is an Indexed bibliography.
Finally, guidance through the three volumes Is offered in the form
of the Foreword, Project General Summary and Tables of Contents
•-in each of the three volumes.
The authors wish to acknowledge the many helpful comments and
suggestions of the NAPCA Project Officer, Mr. George L. Huffman.
The salient features of the project are summarized briefly below.
Expansion and details are given In the texts of Volumes Land II.
The main objectives of the program were:
a. Search all available literature for pertinent Infor-
mation relative to the datalytlc oxidation of sulfur
dioxide, i.e., active materials, mechanisms of catal-
ysis, methods of application, equipment employed, etc.
Identify, describe and evaluate processes disclosed
in the literature to have commercial potential for
removal of sulfur dioxide from flue gas by oxidation.
b. Test, in the laboratory, candidate materials and
methods suggested in the literature for potential ap-
plication to removal of sulfur dioxide from flue gas
by catalytic oxidation.
c. Identify at least one effective catalyst for the de-
sired application and design a process for removal
of sulfur dioxide from flue gas by catalytic oxida-
tion and recovery of the sulfur value.
An intensive search of the literature revealed the following:
a. The transition metal oxides, notably vanadla, and
platinum were the most commonly employed solid
catalysts for practical conversion of sulfur dioxide
to trloxlde. Nitrogen dioxide was the only practi-
cal gaseous catalyst noted.
b. Kinetic equations describing conversions of sulfur
dioxide over vanadla or platinum catalysts were de-
rived from data relative to commercial production
of sulfuric acid, I.e., high concentrations of
sulfur dioxide. There was nothing available to
describe results at the comparatively low concen-
trations of sulfur dioxide found in flue gas.
c. A number of processes were described as having com-
mercial potential for flue gas cleaning. Compara-
tive cost-performance evaluation of these oxidation
processes eliminated all but two types as having
realistic commercial poVnutlal, viz., one type based
on vanadia catalyst and i-m- based on nitrogen dioxide
catalyst.
11
• MONSANTO RESEARCH CORPORATION •
III
. ,• MONSANTO RMBANCM CORPORATION •
-------
d. The moat practical mode of recovery of oxidized sulfur
value from a use standpoint, In this country. Is produc-
tion of fertilizer grade sulfurlc acid.
Laboratory tests and comparative evaluation of commercial and
experimental catalysts indicated the following:
&. Commercial vanadla catalysts employed in production of
sulfurlc acid are effective In converting sulfur dioxide
at concentrations found in flue gas.
b. Although platinum catalyst performance is essentially
equivalent to that of vanadla, a cost-performance
comparison indicated vanadla is ten times more effective.
c. No other candidate materials were shown to be as effect-
ive as vanadla, platinum or nitrogen dioxide in convert-
Ing sulfur dioxide to trloxide.
d. Nitrogen dioxide was the only practical "low temperature"
catalyst observed.
e. Using nitrogen dioxide as a catalyst, It Is potentially
practical to remove both sulfur dioxide and indigenous
nitrogen oxides from flue gas simultaneously.
From preliminary process designs and cost estimates, based on
laboratory data generated In this program, the following emerge:
a. Processes, based on vanadla catalyst, for oxidizing
sulfur dioxide and removing it from power plant flue
gas, as sulfurlc acid, are likely to cost in the range
of $12 to $25 of capital per Installed Xw of power plant
capacity. A large portion of the cost results from the
need for corrosion resistant equipment.
b. Operating costs for vanadia based processes are likely
to be in the range of 0.50 to 0.7') mllls/Kw-Hr generated
before sulfur value net back.
c. A substantial reduction in capital and operating costs
are potentially available through a technique of surb-
ir.g the oxidized product gas from the main flue gas
stream and recovering It separately.
d. The vanadia based processes are better suited to proposed
new power plant .installations than to existing plants
because of numerous difficulties in retro-fit to
existing power plants.
VOLUME III
TABLE OF CONTENTS
I. INTRODUCTION
II. SECTION 1. AUTHOR INDEX
ill. SECTION 2. KEY WORD INDEX
IV. SECTION 3. BIBLIOGRAPHY LISTING
Page
Tab 1
Tab 2
Tab 3
iv
• MONSANTO RESEARCH CORPORATION •
CORPORATION •
-------
I. INTRODUCTION — VOLUME III
Information accumulated during the literature search phase of
the project has been organized and Indexed on a key-word-in-
context (KWIC) basis. The first section Is an alphabetical
listing of authors with a corresponding bibliography number.
The second section consists of a Key Word Index with a related
listing of titles and corresponding bibliography numbers. The
final section consists of a listing of the bibliography numbers.
For each of these Is given: author, title, Journal reference,
and Chemical Abstracts reference.
Thus, If one knows the author's name only, he would enter the
first section to find the bibliography number, or numbers.
Identifying the author, and, with these numbers, enter the third
section to determine the title of the author's article and the
reference.
On the other hand, if one wishes information relative to, say
platinum catalysts, he would look in Section 2 under PLATINUM,
or similar key word, and scan the corresponding titles. If one,
or a number, seemed directly pertinent, the bibliography number,
or numbers, for the title would be used to enter Section 3 to
identify the reference.
1
• MONSANTO RESEARCH CORPORATION •
-------
AUTHOR INDEX
JO/27/69
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10/27/69
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10/27/69
PAGE
10/27/69
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-------
10/27/6
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10/27/iSS
PAGF. 12
10/27/69
PAGE
13
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-------
:•:/ 27/69
PAGE
10/27/69
PAGE 15
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PAGE 17
HARAH 60TCO
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-------
10/27/69
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10/27/69
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PAGE
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10/27/69
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10/27/69
PINES H
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PAGE 24
ELEYDD67AIC
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-------
10/27/69
PINES H
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RODED 68LAS
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.
RAMAV A7CRK
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10/27/69
PA
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RIOOLER ES
RIDGE D
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BIENAECKER G
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RIGHTMIRE RA
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RITTER LG
RIVOLA L
ROBERTS GH
ROBERTSON TJ
ROBINSON PL
ROBSON S
RODEWALO 0
ROEOER U
ROEGENER H
ROGERS CE
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ROITER VA
PAGE 25
REBIPA64INS
REESRL RSD
KRAUHH68SOR
REINLU65SAS
REINLU66GAC
AOAHM 66BSC
RESHSH66RBC
SOKOAM66DOC
REUBBG60ANM
FERRG 66IFI
FERRG 67EIP
FERRG 67EPG
REZIIG6SPOM
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RIDDES39CCF
RIDGD 49ANM
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RIDLES29RPO
RIFKL 64AEA
RIENG 59TMC
RIENG 64SAC
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LEWIHK26NOT
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RINCJB67CCH
RINCJB67MAI
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RITTLG63ODF
RIVOL 66CBS
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ROBEGH65EFP
AOAMD 66ISR
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ROBSS 28COO
RODED 68LAS
GRUNE 66POI
ROEGH 64MOP
ROGECE66RNB
ROGISZ66SOC
ROGISZ67DCM
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ROITVA58EOT
ROITVA5BTRO
ROITVA60TKO
ROITVA60TMO
ROITVA62IKP
ROITVA65SOC
RZAEPB60KOT
-------
10/27/69
ROLL L
ROSCHIN SE
COSENBLATT EF
RGSENKNOP 7.P
HCSENHAL AL
P.flSSLEK
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p.nussfui we
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ROZFNKNOP ZP
ROZOVSKII AY
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RUDYOK NT
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RUGH AL
RUHR-CHE1IE A.G.
RIJISAKOV HV
RUIZ VP
RUIZHOV VP
RUIZnV VP
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ES
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PUSTAM;IV Ml
RUZICKA S
PYABCHENKDV A I
RYLUNO LB
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S.A.E.S. GETTERS S.D.A.
S.O.G.R.E.A.H.
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AOOVSKII AS
SAFIN RS
SAKAI J
SAKAI W
SAKATft Y
SAKOOYNSKII KI
SALS*S-SF.RRA F
SALTAN'IVA VP
PAGE 26
STAnvP6*KOS
ROLLL ftTROF
ROSCSF66ELP
POSEEF46PPC
VASINA60SRS
KUCZW 59ATI
ROSS 67MOA
ROSS 67TSn
RHTGH 26GOV
GLASV 66COT
MALLHC67FBD
AMELAGA600R
AFANPA38THE
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MUKHIPA7SWR
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REURF 67PIN
RIIGHAL6SPOS
RUHR 62CRD
LIIKYPM33COO
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FPICH 67TSC
41 ICVS'-'-CCP
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10/27/69
SAM01L I
SANOALINAS 0
SANDERS JV
SANORAK VR
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SANTOS AH
SARKITS VB
SAROCH V
SATAVA V
SATSltK AF
SATTERFIELD CN
SAVELSBERG U
SAVINKOVA El
SAHARA Y
SCHCHUKIN ED
SCHEIOEL C
SCHEVE E
SCHEVE J
SCHLESINGER CB
SCHMAHL NG
SCHNEIDER P
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SCHOENHERR S
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SCHRADER R
SCHREIBER F
SCHREINER HC
SCHULER RW
SCHUMANN
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SCHWAB GH
SCHHALB H
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SCHHARZENBEK EF
SCHHENK W
SCHYTIL F
SCOTT MD
SEAVER PH
S PDAS NEVA EG
SEFCIK H
SEFEROVIC B
SEGAL AY
SEHNOUTKA J
SEIVAHA T
PAGE 27
SALTVP63VCO
SALTVP6SC
SAHOI 680CT
SANDO 63SCI
SANDJV64RBR
NORDBI67POS
SANSJ 36DSC
YANEJF6SPAS
MUKHIP57ACP
NUKHIP63TUO
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SAROV 66SRF
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EREMVY38IOC
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ROBEGH65EFP
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MORIS 65ESG
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SCHEC 64RIM
RIENG 64SAC
SCHEJ 6AEAO
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SCHRR 64EOI
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LAMHC 66SAC
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SCHVF 61DOT
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SEIVT 61TCO
-------
10/27/60
r.n.
SELIG HJ
SFLIGA M
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BV
SHRSIB^AN SS
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PAGE 28
SEIYT 66DSC
SELO 27CPO
SEL IHJ67PSF
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10/27/69
SMIOOVICH EV
SMITH RI
SOC. GENERALE MET ALLURGIOUE DE HQBCIKEN
SOCIETE ANON. OES MANUFACTURE OES GLACES ET PRQOUITS . . . .
SOCIETE GENERALE DE PROOUITS REFRACTORIES .........
PAGE 29
STEGJF55VOO
SIEH 65SAC
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SILI 33C
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SIHEA 66COT
VOSOJ 65SSD
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MESAS 66POF
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SOCIET56000
SOC I 65PQC
POZIME64POS
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PIERRJ66RPL
KUNITI63AOT
SOLOBI64EOC
SOLOBI64TIO
NEUMB 35DPO
-------
10/27/69
30
10/27/69
PAGE 31
SC50KINA NM
VE
SOSEKINA GV
SPAITE PW
SPENCE P
SPENGLER G
SPERANSKII BA
SPEVAKQVA KA
SPITSYN VI
SOUIRFS AH
STABILINI HP
STADNIK PW
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STAIB M
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STEADMAN JF.
STEGER JF
STELLING PH
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STETTER G
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STOEWENER F
STOlft
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1C/27//S1
THOOflS G . . . .
THOMAS HJ . . . .
TIKHON3V AV . . . .
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TINKLER JD . . . .
TIPPER CFH . . . .
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TITAN I T . . . .
TITLESTAD N . . . .
TKACH YA . . . .
TODES OH . . . .
TOGO N . . . .
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TOMAS1K Z . . . .
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TOMKOVA 0 . . . .
TONE S . . . .
TORIUMI T . . . .
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TOVMAS'YAN IK . . . .
TOYO KOATSU INDUSTRIES,INC.
TRABER OG . . . .
TRAPLY G
TRAHINSKI S
TREJO A
TRENHITH AB
TRIKILO AI
TRIMN OL
TSEITIN AN
TSEITLIN AN
TSURIKOV SA
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U.S. OEPT. OF INTERIOR, BUR. OF MINE S, WASH. O.C .
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PAGE
32
OAVIR 64KCO
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10/27/69
VAHEPVUORI TK
VAN POOL J
VANDAGE C
VARLAMOV ML
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WAY OF
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WOLFEN
UNO. .METALLURGISCHE PRODUCTION
IV
PAGE 33
VAHETK67SAA
VAN J 65RCH
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-------
10/27/69
WE I HER P
WFIL JA
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PAGE 34
HOEHH 671 QT
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-------
KEY WORD INDEX
10/27/69
ABSORBENT
ABSORBER
ABSORBERS
ABSORBING
ABSORPTION
PAGE
INCREASING THE MECHANICAL STRENGTH OF POROUS DISPERSE BODIES
ANTIPOLLUT ION PROCESS USES ABSORBENT TO REMOVE
SULFUR-DIOXIDE FROM FLUE-GASES
POLYMER ABSORBENT FOR " " ~"
LUDWS 68APV
SULFUR-DIOXIDE THAT PROMOTES ITS
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CONTINUOUS REMOVAL OF SULFUR-DIOXIDE FROM GAS MIXTURES
BY A FLUIDIZED LAYER OF SOLID GRANULAR ABSORBENT
ZEnSIF65CRS
ON THE ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE
SOLUTION IN A VENTURI ABSORBER ELEND 66ASD
HYDRODYNAMICS AND MASS TRANSFER IN A NOZZLELESS VF.NTURI
ABSORBER ABSORPTION OF SULFUR-DIOXIDE INTO WATER
AND MATER SOLUTIONS OF SURFACE ACTIVE AGENTS 66HMT
REGENERATION OF A SULFUR-DIOXIDE ABSORBER MATERIAL
REGENERATION OF AN ABSORBER FOR SULFUR-DIOXIDE
THE ABSORPTION OF SULFUR-TRIOXIDE IN BUBBLE CAP PLATE
ABSORBERS FOR THE PRODUCTION OF OLEUM AKSEYV64TAO
ABSORBING SULFUR-DIOXIDE ON DRY ION-EXCHANGE ROSINS
THE ABSORPTION OF SULFUR-TRIOX IDE IN BUBBLE CAP PLATE
ABSORBERS FOR THE PRODUCTION OF OLEUM AKSEYV6VTAO
STRUCTURAL .CHARACTERIZATION OF CATALYSTS I NTERPRETATI ON
OF DATA ON GAS ABSORPTION ASENJ 67SCP
ABSORPTION OF SULFUR-DIOXIDE AND SEPARATION OF ASHES FROM
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ABSORPTION AND ENERGETIC PROPERTIES OF METALLIC CATALYSTS
SPECIFIC SURFACES OF CATALYSTS BALAAA67AfP
ABSORPTION OF SULFUR-DIOXIDE IN AN UNPACKED COLUMN WITH JETS
ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE AQUEOUS
SOLUTION FRflN A GAS MIXTURE BLASH 66ASO
ABSORPTION OF SULFUR-TRIOXIDE IN A FOAM TYPE APPARATUS
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B L Y AI Go 6 A S T
CATALYTIC PROCESS FOR THE MANUFACTURE OF SULFURIC-ACID IN
SEVERAL CONTACT AND ABSORPTION STEPS CHEM 66C PF
MASS TRANSFER COEFFICIENTS DURING THE ABSORPTION OF SO2
FROM GASES BY AMMONIUM-SULFI TF-BI SULFI TE SOLUTIONS
CHc
ON THE ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE
SOLUTION IN A VENTURI ABSORBER ELFND 66ASD
AN AUTOMATIC CONTROL SYSTEM FOR THE DRYING AND ABSORPTION
CYCLE IN SULFUR IC-AC ID PRODUCTION IGREV 67ACS
SIMULTANEOUS ABSORPTION Of HYDROGEN-SULFIDE AND
S02 BY AMMONIUM-SIILFITE-BISULFITE SOLUTIONS UNDER
SEMI-COMMERCIAL CONDITIONS IVAND 64SAH
-------
10/27/&9
ABSORPTION
ABSORPTIVE
ACCELERATED
ACCELERATING
ACCELERATIONS
ACTIVATED
PAGE
APPARATUS FOR FAST DETERMINATION OF THF ACTIVITY OF
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MACAJ 67AFD
GAS ABSORPTION APPARATUS MELLRA66GAA
ABSORPTION OF SULFUR-DIOXIDE FROM GAS META 62ASD
ABSORPTION OF SULFUR-DIOXIDE BY CALCIUM-HYDROXIDE SLURRY
MISAY 67&SO
MASS TRANSFER AND ABSORPTION WITH REACTION IN ROTARY
TYPE EQUIPMENT NIKON 66MTA
RECOVERY OF SULFUR-DIOXIDE FROM RESIDUAL GASES BY WET
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RATE OF ABSORPTION OF SOLUBLE GASES IN A WETTED WALL TUBE
ABSORPTION OF S03 BY SULFURIC-ACID-MONOHYDRATE
RAMMVM65RAS
THE SIMULTANEOUS ABSORPTION OF SULFUR-OXIDES AND ONE OR MORE
REDUCED SULFUR COMPOUNDS FROM INDUSTRIAL GASES ESPECIALLY
FLUE-GASES REINLU65SAS
REGENERATION OF MAGNESIUM-BISULFITE PULPING LIQUOR AND
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ROGECE66RMB
CHANGES IN THE CONDUCTIVITY AND WORK-FUNCTION OF THE
ELECTRON UPON ABSORPTION OF 0 AND SH2 AND V205 LAYERS
SURNLN65CIT
ABSORPTION OF SULFUR-DIOXIDE TAKEN 64ASD
A NEW ABSORPTION PROCESS TERNAI62NAP
ABSORPTION OF SULFUR-DIOXIDE IN AN IDEALLY MIXED LAYER
VINNLI67ASD
GAS ABSORPTION BY MULTISTAGE VENTURI SCRUBBERS
VOLGBP64GSM
ABSORPTION OF SULFUR-DIOXIDE BY AMMONIUM-SULFITE-BISULFITE
SOLUTIONS IN A SPRAY TYPE VFNTURI SCRUBBER
VOLGBP66ASD
EFFECTS OF SURFACE ACTIVE IONS ON ABSORPTIVE AND CATALYTIC
PROPERTIES OF PT AND PO ZAKUGD66EOS
THE RELATION BETWEEN ACCELERATED CORROSION TESTS AND
OUTDOOR EXPOSURE TESTS OF ELECTROPLATED COATINGS
SUGAS 65RBA
THE RELATION BETWEEN ACCELERATED CORROSION TESTS AND OUTDOOR
EXPOSURE TESTS OF ELECTROPLATED COATINGS SUGAS 65RBC
ACCELERATING CATALYTIC REACTIONS BY RAPID MOVEMENT OF THE
MATERIALS KIPPHR19ACR
ACCELERATING CATALYTIC REACTIONS BY RAPID MOVEMENT OF THE
MATERIALS KIPPHB24ACR
ACCELERATIONS OF CHEMICAL REACTIONS BY VIBRATION
STELP053AOC
MECHANISM
_ ... OF OXIDATION OF SULFUR-DIOXIDE IN THE PRESENCE
OF ACTIVATED VANADIUM CATALYSTS INFLUENCE OF AN
ADMIXTURE OF SALTS OF ALKALI ELEMENTS AND AMORPHOUS
SILICIC-ACID BOREGK40KOO
10/27/69
ACTIVATED
ACTIVATING
ACTIVATION
ACTIVATORS
ACTIVE
PACE
MECHANISM OF THE OXIDATION OF SULFUR-DIOXIOE IN THE PRESENCE
8F ACTIVATED VANADIUM CATALYSTS
OMPQUNDS UNDER THE CONDITION OF
»CTlVATEp_yANADIUM_C.ATALYSTS_ jugJug} fcljj ,g-
ROREGK40MOT
EFFECT OF TEMPERATURE ON THE RATE OF FORMATION OF SUIFURIC
BY THE OXIDATION OF SULFUR-DIOXIDE ON AC'TIVATEO CARBON BY
INVESTIGATION OF THE MECHANISM OF OXIDATION HYDROGENATION
AND ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS
OXIDATION OF SULFUR DIOXIDE ON ACTIVATED CARBON AT 20-DEG
IN THE PRESENCE OF HATER VAPOR OAVTOK61IMO
POROUS ACTIVATED ALUMINA OF HIGH MECHANICAL STRENGTH
HUTTJC65PAA
ULTRASONICALLY ACTIVATED CATALYSTS FOR CHEMICAL REACTION
JONEJB66UAC
OXIDATION OF SULFUR-DIOXIDE ON ACTIVATED CHARCOAL BY LIQUID
CONTACT METHOD OVCHEN560SD
S02 OXIDATION ON MECHANICALLY ACTIVATED V205 PAUDR 6SSOO
THE MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE INFLUENCE OF TEMPERATURE AND TIME OF CARBON
DESORPTION ON ADSORPTION AND OXIDATION OF H2S AND S02
SIEOJ 64MCO
REMOVAL OF S02 FROM GASES. BY USING VARIOUS GRADES OF
ACTIVATED CARBON SIEDJ 64RSG
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE CONTRIBUTION OF CARBON FREE-RADICALS IN THE
DATION PROCESS
IEDJ 65MCO
TO S03 OXIDATION PRO
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THE CONCENTRATION OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND S02 OXIDATION
PROCESSES
CATALYSIS BY ACTIVATED ADSORPTION
ACTIVATING CATALYSTS
_.EDJ 66MCO
TREJA A5CBA
HQRSGFA6AC
EFFECTS OF CARRIERS AND DILUENT ON THE ENERGY OF ACTIVATION
AND THE VALUE OF THE DISPERSION COEFFICIENT
RELATION BETWEEN REACTION ORDER AND ENERGY OF
OF DIRECT AND INVERSE REACTIONS
ACTIVATION OF CATALYSTS
COMPARATIVE RESULTS FOR THERMAL AND ELECTRONIC
MIXTURES OF SULFUR-DIOXIDE AND OXYGEN
ENERGETIC ACTIVATION OF ADSORPTION CATALYSTS
ADAOIE36ECO
ACTIVATION
ROREGK45RRR
HORSGF47AOC
ACTIVATION OF
MOYEAJ65CRF
PARYT 67EAO
THE REACTION MECHANISM IN THE CONTACT SULF URIC -ACID PROCESS
AND THE METHOD OF ACTION OF ACTIVATORS NEIIMB 29TRM
HYDRODYNAMICS AND MASS TRANSFER IN A NOZZLELESS VENTURI
ABSORBER ABSORPTION OF SULFUR-DIOXIDE INTO WATER
AND WATER SOLUTIONS OF SURFACE ACTIVE AGENTS
ELEND 66HMT
ENTROPY OF THE ACTIVE COMPLEX IN THE OXIDATION OF
SULFUROUS-ANHY.DRIDE OVER PT CATALYST GOLPGI63EOT
38
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10/27/69
ACTIVF
ACTIVITIES
ACTIVITY
PAGE
PHASE CONDITION OF ACTIVE COMPONENT IN VANADIUM CATALYSTS
OF SULFUR-DIOXIDE OXIDATION ILLAVV55PCO
REACTION OF SULFUR-DIOXIDE WITH ACTIVE NITROGEN
ACTIVE CENTER OF A CATALYST KIYQR 40ACO
REACTIONS OF OXIDE CATALYSTS WHOSE OXYGEN EXCHANGES WITH THE
SUBSTRATE OXYGEN AND DEFINITION OF ACTIVE METAL OXIDE
ACTIVE FORM OF MANGANESE CATALYST IN THE OZONE CATALYTIC7"00
METHOD OF OXIDATION OF SULFUR-DIOXIDE IN ACID SOLUTIONS
A NEW APPROACH TO THE STUDY OF ACTIVE CENTER OF CRYSTALLINE0
CATALYSTS POLTOM66ANA
CHEMICAL DEPOSITION OF CATALYT1C ALLY ACTIVE PLATINUM ON
.r-GRAPH-I-TE-AND' METALLIC POWDERS AND SURFACES RHODRN67CDO
DETERMINATION OF THE NUMBER OF ACTIVE CENTERS ON THE CARBON
SURFACE BY THE ELECTROCHEMICAL METHOD IN OXYGEN
CHEMISORPT10N SIEDJ 650NA
NEW METHOD FOR DETERMINING THE COMPOSITION OF THE ACTIVF.
CENTER OF A METALLIC CATALYST STREZV67NMD
EFFECTS OF SURFACE ACTIVE IONS ON ABSORPTIVF AND CATALYTIC
PROPERTIES OF PT AND PD ZAKIIG066EOS
PLATINUM METAL ALLOYS IN ELECTROCATALYSIS A FURTHER
EVALUATION OF RELATIVE ACTIVITIES BROOEW66PMA
EFFECT OF CARRIERS ON THE ACTIVITIES AND PROPERTIES OF
VANADIUM CATALYSTS FOR THE OXIDATION OF SULFUR-TRIOX IDE
SOLOBI64EOC
DEPENDENCE OF THE CATALYTIC ACTIVITY OF THF
V205 ON ITS MODE OF COMBINATION WITH SILICA
ADADIE29DOT
INFLUENCE OF THE COMPOSITION AND THE DISTRIBUTION OF THE
CATALYTIC MASS ON THE ACTIVITY OF CHROMIUM CATALYSTS
AOADIE34IOT
ACTIVITY OF SOLID CATALYSTS ARGOWB53AOS
MOBILITY OF OXYGEN AND CATALYTIC ACTIVITY OF OXIDES IN
RELATION TO. OXIDATION.RE ACTIONS BOREGK66MOO
SPEC
1C CATALYTIC ACTIVITY OF METALLIC PLATINUM
THE SPECIFIC CATALYTIC ACTIVITY OF METALS SULFUR-DIOXIDE
OXIDATION ON PLATTMIM CATALYSTS CHESVS5STSC
THE CATALYTIC ACTIVITY OF PLATINIZED NICKFL IN THE OXIDATION
OF SULFUR-DIOXIDE OAVTHK6ITCA
THE MECHANISMS OF OXIDATION HYOROGENATION AND
ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS RELATION
BETWEEN DEPOLARIZING OXIDES ADSORBED ON CARBON AND
PLATINUM AND THE CATALYTIC ACTIVITY IN THE OXIDATION OF
SULFUR-DIOXIDE OAVTOK61TMO
CATALYTIC ACTIVITY OF SIIPPDRTEH PLATINUM DciiGNA65CAn
SPECIFIC ACTIVITY OF OXIIlf CATALYSTS 0/ISVAA4SAO
INFLUENCE OF CARBON-MllNMX 1 Of ON THE ACTIVITY OF PLATINUM
CATALYSTS DURING THI OXIDATION, OF SULFUR-DIOXI OF TO
SIILFUR-TRIOXIDF ERFMVYSHIOC
39
10/27/69
ACTIVITY
PAGE
ACTIVITY STRUCTURE AND ELECTRICAL PROPERTIES OF MI.XF.D
EFFECT OF PORE GEOMETRY ON THE ACTIVITY AND
EFFECTLOFTPOTASSIUM-OXIDE ON THE ACTIVITY OF VANAofuM0 67EPG
CATALYSTS IN THE OXIDATION Of SULFUR-DIOXIDE AT LOW
TEMPERATURES GERBEV63EOP
THE EFFECT OF METAL OXIDE ADMIXTURES ON THE ACTIVITY OF THE
TIN CHROMIUM CATALYST GFRNOV35TEO
EFFECTS OF POISONS ON POROUS CATALYST ACTIVITY
GIOLF 67EOP
EFFECT OF POISONS ON POROUS CATALYST ACTIVITY
GIOLF 67EPP
EFFECTS OF INITIAL CONDITIONS ON THE STEADY STATE ACTIVITY
OF CATALYST PARTICLES HARTJS67EOI
THE INFLUENCE OF SMALL QUANTITIES OF ADDED PLATINUM ON THE
CATALYTIC ACTIVITY OF VANAOIUM-PENTOXIDE REGARDING THE
OXIDATION OF HYDROGEN ILCHNI67TIO
A CRITIQUE ON THE ACTIVITY TEST OF COMMERCIAL CATALYSTS
V205 CATALYSTS ISHIT 66ACD
THE VARIATION WITH TEMPERATURE OF THE CATALYTIC ACTIVITY
OF AN OXIDIZED STAINLESS STEEL SURFACE IN THE OXIDATION
OF SULFUR-DIOXIDE JACKPJ59VTC
INFLUENCE OF ALKALI SULFATED ON THE ACTIVITY OF
V205 IN THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
EFFECT OF ALKALI METAL SULFATES ON THE ACTIVITY OF RUP
V205 FOR THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
JIRUP 61EAM
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVITY OF
OXIDATION OF
ITY OF
VANAOIUH-PENTOXIDE IN'THE'CATALY
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVI
VANADIUM-PENTOXIDE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE JIRUP 63VPC
CATALYST AND ENZYME THE PROBLEM Of SURFACE ACTIVITY OF
NATURAL SUBSTANCES KOBPNISSCAE
INFLUENCE OF THE ULTRASONIC FIELD ON THE CATALYTIC ACTIVITY
OF MN02 PREPARED BY ELECTROLYSIS KOWAE 65IUF
EFFECT OF NUCLEAR RADIATION ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE REACTION OF S02 OXIDATION KOZAZ 66EON
CATALYTIC ACTIVITY OF VANADIUM-PENTOXIDE CATALYST ON
KUBOT 54CAO
ACTIVITY OF THERMALLY STABLE VANADIUM CATALYSTS FOR THE
OXIDATION OF SULFUR-DIOXIDE KUNITI63AOT
THE CATALYTIC PROPERTIES OF NONPLATINUM CATALYSTS IN THE
OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TR
HACTIVjTY.P.F_IRgN-CgPPER ' ~ ~
I0X1DE THE
THE
______
CATALYSTS KURI
IVITY OF CHROMIUM-OXIDE STANNIC-OXIDE CATALYSTS
THE OXIDATION OF S02 TO S03
THE CATALYTIC ACTIVITY OF METALS
INFLUENCE OF ARSENIC ON THE CATALYTIC
FOR THE OXIDATION OF SULFUR-DIOXIDE
KURINP56ACO
LANDMA6ATCA
ACTIVITY OF PLATINUM
MAXTEB28IOA
1*0
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1C/27/69
ACTIVITY
ADDITIVES
ACIABATIC
THE INFLUENCE OF THE CARRIER .
CATALYSTS FOR THE OXIDATION OF
PAGE
THE STRUCTURE ANO ACTIVITY OF HETEROGENEOUS CATALYSTS
EFFECT OF WATER VAPOR AND IRON COMPOUNDS ON THE ACTIVITY
OF VANADIUM CATALYSTS IN A FLUIDIZED-BED MUKHIP63EOW
IMPROVING THE ACTIVITY OF OXIOIC CATALYSTS NIXHWB63IAO
RELATION BETWEEN CATALYTIC ACTIVITY OF SOME METALS AND THEIR
SUBLIMATION HEATS RESHSM66RBC
SEMICONOUCTANCE AND CATALYSIS RELATION BETWEEN
CATALYTIC ACTIVITY STOICHIOME TRIC COMPOSITION AND STATE
OF ELECTRON LINKAGE FOR N-CONDUCTING MIXED CATALYSTS OF
THE HOPCALITE-TYPE III. RELATION BETWEEN CATALYTIC
ACTIVITY STOICHIOMETRIC COMPOSITION AND RATE OF ELECTRON
LINKAGE FOR P-CONDUCTING MIXED CATALYSTS OF THE HOPCALITE
TYPE . RIENG 6'(SAC
EFFECT OF CATALYST POISONING ON THE OVERALL SELECTIVITY AND
ACTIVITY SADAE 67EOC
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THE CONCENTRATION OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND S02 OXIDATION
PROCESSES SIFDJ 66MCO
DEPENDENCE OF CATALYTIC ACTIVITY OF METAL ON THEIR POSITION
IN PERIODIC TABLE SOKOAM66DOC
__ THE Cft,R,ER ON THE ftcT|viTY OF THF VANADIUM
SULFUROUS-ANHYORIDE
SOLOBII>4TIO
METHODS OF TESTING THE ACTIVITY OF CATALYSTS STADVP64MOT
COMPARATIVE CATALYTIC ACTIVITY OF CENTERS ON THE SURFACE OF
CRYSTALS AND OF AN INERT CARRIER STREZV64CCA
VANADIUM CATALYST USED IN THE OXIDATION OF S02 EFFECT OF
MECHANICAL TREATMENT OF CARRIER ON THE ACTIVITY OF CONTACT
SWINA 66VCU
GENERAL RULE OF THE CATALYTIC ACTIVITY OF METALS
TANAK 66GRO
INFLUENCE OF RADIATION REACTIVITY AND CATALYTIC ACTIVITY OF
SOLIDS TAYLEH64IRR
EFFECT OF PARTICLE SIZE OF A VANADIUM CATALYST ON ITS
ACTIVITY IN THE FLUIDIZED-BED OXIDATION OF SULFUR-DIOXIDE
TRABDG59EOP
ACTIVITY OF PURE VANADIUM-P£NTOXIDE IN CONTACT OXIDATION OF
S02 WEYCS 65AOP
INFLUENCE OF SORPT10N ON THE ACTIVITY HF PURF V205 IN THE
OXIDATION OF S02 WFYCS h6I OS
EFFECT OF AOD1TIVF.S ON OXIDE CATALYSTS SE MI CONDUCT IVITY
AND CATALYSIS QUANTUM ASPECTS OF CATALYSIS
ILLUSTRATED BY INVESTIGATIONS USING MIXED OXIDE CATALYSTS
STHEJ 64E40
TYPES OF CORROSION UNO BEHAVIOR OF METALS AND ADDITIVES IN
BOILER FURNACES WICKK 65TCB
DESIGN OF CONTACT PROCESS EQUIPMENT WITH AN ADIABATIC
CATALYST LAYER FOR THE OXIDATION OF SULFUR-DIOXIDE DESIGN
OF EQUIPMENT WITH THE INTRODUCTION OF COLD REACTION
MIXTURES AND WITH INTERMEDIATE HEAT EXCHANGERS
BFSKVS63DOC
lft/27/M)
ADIABATIC
..OSORBEO
ADSORBENT
ADSORBENTS
AOSORPT ION
PAGE
COMPUTER PROGRAM FOR AN ADIARATIC CATALYTIC REACTOR
CHAMJP6*CPF
COMPUTER PROGRAM FOR AN ADIABATIC CATALYTIC REACTOR
OXIDATION OF.S02 IN AN ADIABATIC CONVERTER
HAMOJP66CPA
.502 IN AN ADIABATIC CONVERTER KAOLB ft6ons
OPTIMIZATION OF AN AOIARATIC STAGE REACTOR LANGD 6400A
CONTROL OF A COLD SHOT ADIABATIC BED REACTOR WITH A
DECAYING CATALYST LEE KY63COA
OPTIMAL ADIABATIC BED REACTORS FOR SULFUR-DIOXIDE WITH COLD
SHOT COOLING r " ~-~
THE APPLICATION OF A GRADIENT METHOD TO THE OPTIM
AOIABATIC MULTISTAGE CATALYTIC REACTORS
GRAPHICAL TECHNIQUES FDR AOIABATIC STAGED SYSTEMS
LEF KY630AB
IZATION OF
LUQUF 67TAO
MEISHP60GTO
STABLE AND UNSTABLE BEHAVIOR OF ADIABATIC TUBULAR REACTOR
AS FOR EXAMPLE IN CATALYTIC CO OXIDATION PAOBG 67SAU
FIVE-STAGE ADIABATIC CONVERTER FOR OXIDATION OF
SULFUR-DIOXIDE SHAPLIS9FSA
COMPUTATION OF THE ADIABATIC TEMPERATURE FOR THE OXIDATION
OF SULFUR-DIOXIDE SIMFA 66COT
THE COMPUTATION OF CONTACT APPARATUS FOB THE OXIDATION OF
SULFUR-DIOXIDE ON AN AOIABATIC CATALYST LAYER
THE MECHANISMS OF OXIDATION HYDROGENATION AND
ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS RELATION
BETWEEN DEPOLARIZING OXIDES ADSORBED ON CARBON AND
PLATINUM AND THE CATALYTIC ACTIVITY IN THE OXIOATION OF
SULFUR-OIOXIOF. flAVTOKMTMO
IMPROVEMENT OF THE MASS TRANSFER FROM A GAS TO A POROUS
CATALYST OR ADSORBENT BY PRESSURE OSCILLATIONS
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INVESTIGATIONS OF POROUS ADSORBENTS AND CATALYSTS PY MEANS
OF DISTRIBUTIVE FUNCTIONS OF THF SURFACE WITH REGARD TO
ITS CURVATURE SUKUI 661 PA
USE OF CERTAIN CATALYSTS AND ADSORBENTS IN INDUSTRIAL
HYGIENE PRACTICE AND IN PRODUCTION KOTFNZS6UOC
INCREASING THE MECHANICAL STRENGTH OF POROUS DISPERSE BODIES
ADSORBENTS AND CATALYSTS RFBIPA64IMS
ADSORPTION AND ENERGETIC.PROPERTIES OF METALLIC CATAIYSTS
ANOMALIES CAUSED BY THE SLOW ADSORPTION OF A RF.ACTANT ON THF
COURSE OF CERTAIN TYPES OF CONSECUTIVE ANO RKANCHfO
HETEROGENEOUS CATALYTIC REACTIONS RFRAL 67ACB
ASPECTS IN THE INVESTIGATION OF ADSORPTION ANO CATALYTIC
PROCESSES BLIZG f>SAIT
OXIDATION OF SP2 BY 02 OR O2-03 MIXTURE IN THF PRFSENCF OF
SILICA-GEL ADSORPTION OF 02 ON SILICA-GEL ALUMINA-GEL AND
COTTON BPINE 4100S
ADSORPTION STUDIES OF PLATINUM-SUPPORTED CATALYSTS
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10/27/69
ADSORPTION
AGENTS
AGING
AIR
PAGE
UTILIZATION OF DILUTE ADSORPTION CATALYSTS IN THE CHEMICAL
INDUSTRY
PURIFICATION OF GASES BY SOLID ADSORPTION
ENERGETIC ACTIVATION OF ADSORPTION CATALYSTS
ADSORPTION EQUILIBRIUMS AND REACTION SEQUENCES IN THE
KOBONI57UDD
MITS 67POG
PARYT 67EAO
HETEROGENEOUS CATALYTIC REACTIONS RIEKL 64AEA
THE MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE INFLUENCE OF TEMPERATURE AND TIME OF CARBON
DESORPTION ON ADSORPTION AND OXIDATION OF H2S AND S02
CATALYSIS BY ACTIVATED ADSORPTION
A STUDY OF ADSORPTION ISOTHERMS ON OXIDE FORMS OF
METALSIL ICATE CARRIERS AND CATALYSTS
SIEDJ 64MCO
TREJA 45CBA
ZULFZG66SAI
HYDRODYNAMICS AND MASS TRANSFER IN A NOZZLELESS VENTURI
ABSORBER ABSORPTION OF SULFUR-DIOXIDE INTO WATER
AND WATER SOLUTIONS OF SURFACE ACTIVE AGENTS
ELEND 66HMT
POWDERED METAL REACTION AGENTS PARTIALLY EMBEDDED IN METAL
SUPPORTS SAES 66PMR
EFFECT OF PORE GEOMETRY ON THE ACTIVITY AND AGING OF
CATALYSTS FERPG 67EPG
AIR POLLUTION CONTROL IN PETROLEUM REFINERIES
APAIK 67APC
SOLUTION TO THE S02 PROBLEM IN AIR PURIFICATION BY
OPERATIONAL AND INDUSTRIAL MEASURES BROKW 66STT
PREVENTION OF LOW AND HIGH-TEMPERATURE CORROSION AND
DEPOSITS IN OILrFIRED STEAM BOILERS RY COMBUSTION
SL" "
WITH LOW AIR SURPLUS
CHAIM 66PLH
AIR POLLUTION FROM POWER STATIONS CRAXSR66APF
CATALYTIC COMBUSTION OF GASEOUS IMPURITIES IN WASTE AIR
FOULA 55CCO
CONTROL OF AIR POLLUTION FROM LARGE THERMAL POWER STATIONS
GARTFE66COA
PHOTOCHEMICAL OXIDATION OF SULFUR-DIOXIDE IN AIR
GERHER55POP
SNPA'S PROCESS FOR H2SCK PRODUCTION DEVELOPED WITH EYE ON
AIR POLLUTION GUYAGLSSSPF
ECONOMIC ELIMINATION OF AIR POLLUTION THROUGH RECOVERY
PRODUCTS IN POLYESTER GAS SCRUBBERS HAMPNH65EEA
USE OF A SULFUR-DIOXIDE SCRUBBING SYSTEM IN AIR POLLUTION
CONTROL LAWLWC USD
EFFECT OF FUEL CHARACTERISTICS AND EXCESS COMBUSTION. AIR
ON SULFURIC-ACID FORMATION IN A PULVERIZED COAL-FIRED
BOILER LEE GK67EFC
PREVENTION OF AIR POLLUTION A PRESSING DFMAND FOR CHFMISTRV
AND ECONOMY LFITW 67POA
PROBLEMS AND CONTROL OF AIR POLLUTION MALLFS PCA
AIR POLLUTION CONTROL MEASURES TAKFN AT THE POWER STATION
IN YOKKAICHI DISTRICT MIYAM 66APC
REHQVAL OF AIR POLLUTANTS FROM GASES RV REACTION WITH
PARTICULATE SOLIDS PRFTST67PAP
10/27/69
AIR
AIR-POLLUTION
ALKALI
ALKALINE
ALKALIZED
ALLOY
ALLOYS
PAGF
OXIDATION OF S02 IN AIR AT 910-OEr.RF.E S COOPERATIVF
INFLUENCE OF CO AND N'l SHAWJTA60
REDUCTION OF AMBIENT AIR CONCFNTPATI ON OF SULFIIR-OXIPES
PRESENT AND FUTURE PROSPECTS SPAIPW66R
SULFUR-OXIDES IN FLUE-GAS AND IN THE ATMOSPHERE A PROBLEM
KEEPING THE AIR PURE SPFNG ftSS
AIR POLLUTION THE CONTROL OF SULFUR-DIOXIDE FRO" POWER
STACKS THE REMOVAL OF SULFUR-DIOXIDE FROM ST.*CKAM*||
AIR POLLUTION IN PETROLEUM REFINING
AIR POLLUTION CONTROL BY OIL REFINERIES
AIR-POLLUTION PROBLEMS OF THE PHOSPHATE INDUSTRY
SUTTP 6BA
TFRMMA66A
SMITRI68A
MECHANISM OF OXIDATION OF SULFUR-DIOXIDE IN THE PRESENCE
OF ACTIVATED VANADIUM CATALYSTS INFLUENCE OF AN
ADMIXTURE OF SALTS OF ALKALI ELEMENTS AND AMORPHOUS
SILICIC-ACID BCRFGK4PM
THE EFFECT OF ALKALI METAL SULFATES ON THE CATALYTIC
PROPERTIES OF VANADIUM D7ISAP61T
INFLUENCE OF ALKALI SULFATED ON THE ACTIVITY HF
V205 IN THE CATALYTIC OXIDATION OF SULFUF -III DXimE
EFFECT OF ALKALI METAL SULFATES ON THE ACTIVITY CF
V205 FOR THE CATALYTIC nxiOATION OF SULFIJP-Dinx IDE
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METAL SULFATES ON THE ACTIVITY GIF
IN THE CATALYTIC OXIDATION OF
J I RlIP 63r
METAL SULFATES ON THE ACTIVITY OF
IN THE CATALYTIC OXIDATION OF ^^
THE"MECHANISM"AND THE KINETICS OF SULFUR-DIOXIDE OXIDATION
ON CATALYSTS CONTAINING VANADIUM AND ALKALI OXIOFS
KINETIC STUDIES OF THE OXIDATION OF SULFUH-OIOXI OF. ON
VANADIUM CATALYSTS PROMOTED BY ALKALI METAL SALTS „„„,,,.
7 AKHHb7> OR
ALKALINE REGENERATION OF VANADIUM FROM SPENT CATALYST FROM
SULFURIC-ACID PRODUCTION RPLPNUfthA
ALKALINE EARTH METAL COMBINATION WITH SP2 HF FLUE-RAS
IN A FLUE DUST CLOUD K*HFM 67A
PROCESS DEVELOPMENT IN REMOVING SULFUR-DIOX IDE FROM HOT
FLUE GASES PILOT PLANT STUDY PF THE ALKALI7FO
ALUMINA SYSTEM FOR SUL FUR-DI OX IDF REMOVAL H1FNO 6 7P
HEHAVIHR OF TOMRAC ALl QY IN SOMF CORROSIVF MEDIA
EFFECT OF THE ALKALI
VANAOIUM-PENTOXIDE
SULFUR-OXIDE
EFFECT OF THE ALKALI
VANADIUM-PENTOXIDE
SULFUR-OXIDE
CATALYSIS OF SULFUR-DIOXIDE TO SULF UR-TRIPXIOE BY METALS A
PLATINUM-GOLD ALLOYS RDRFGK51C
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1C/27/69
ALLOYS
PAGE 10
CATALYSIS OF THE CONVERSION OF SULFUR-DIOX IDE TO
SULFUR-TRIOXIDE RY METALS AND PLATINUM GOLD ALLOYS
30REGK53COT
PLATINUM METAL ALLOYS IN ELECTROCATALYS1S A FURTHER
EVALUATION OF RELATIVE ACTIVITIES
NICKEL SILICON ALLOYS HAYN
POSSIBLE APPLICATIONS OF RHENIUM MF.TAL AND ITS ALLOYS
BROOEW66PMA
H&YNFG67NSA
ALUMINA
ANODIC OXIDATION OF SULFUR-DIOXIDE ON GOLD AND PLATINUM-GOLD
ALLOYS LEZHKAblAOO
NORLE METAL ALLOYS AS ANODE ELECTROCATALYSTS NIEOLW&TNMA
CORROSION OF LEAD ALLOYS IN SULFURIC-ACID PELZVE67CLA
STUDY OF CORROSION OF IRON AND ITS ALLOYS IN CHLORINE AND
SULFUR-UIOXIOE BY THE THFRMOGRAPHIC METHOD TCVKIK66SCI
PURIFICATION OF SULFUROUS RESIDUAL GASES BY ALUMINA BED
AZOUA 64PSP
PROCESS DEVELOPMENT IN REMOVING SULFUR-DIOXIDE FROM HOT
FLUF GASES PILOT PLANT STUDY PF THE ALKALIZED
ALUMINA SYSTEM FOR SULFUR-DIOXIDE REMOVAL BIEND &TPDR
POROUS ACTIVATED ALUMINA OF HIGH MECHANICAL STRENGTH
HUTTJC65PAA
VANADIUM ON ALUMINA CATALYST FOR FLUI01 ZED-BED OXIDATIONS
PROCESS FOR PRODUCING AN ALUMINA CATALYST BASE
ALUMINA-GEL
OXIDATION OF S02 __ _
SILICA-GEL ADSORPTION OF
COTTON
ALUMINOS L CflTEVAN4DIUM MODIFIED CRYSTALLINE ALUMINOSILICATES AND THEIR
PROPERTIES LEVISAhSVMC
ALU"INUVI-CKLORIDE
UTILIZING WASTE FROM THE ALUMINUM-CHLORIDE INDUSTRY FOR
CARRIERS OF PLATINUM IN THE OXIDATION OF SULFUR-DIOXIDE TO
NITT 65VOA
OLECSM66PPA
BY 02 OR 02-03 MIXTURE IN THE PRESENCF OF
~ 32 ON SILICA-GEL ALUMINA-GEL AND
BRINE 4300S
SULFUR-TRIOXIDE
ADADIE34UUF
AMMONIA
OF HASIC ALUMINUM-SULFAT6
B°ETS 5SCOC
EOUILIBRIIIM POSITION AND KINFTICS OF OXIDATION OF
SULFUR-OIOXIDE AND SYNTHESIS OF AMMONIA ANDPL &IEPA
RFACTOR FOR THE OXIDATION OF AMMONIA RISKE 67RFT
AMMONIA RECOVERY FROM WASHINGS OBTAINED DURING THE
PURIFICATION OF SULFUR-DIOXIDE AND SULFUR- TRI OXI OE
CONTAINING GASES THEM 65ARF
FUR
RECOVERY OF SUL
FROM FLIIE-r.AS BY THE USE OF A-MPNIA
MECHANISM FOR RECOVERY OF
CATALYTIC OX IDATION
PLA1INUM LOSSES DURING AMMPNIA
JANIW 67MFR
DEPOSITiNG'METALS ON SILICFPU* CATALYST SUPPORTS FROM AMINE
COMPLEXES IN AQUEOUS AMMONIA SOLUTIONS MULABF&TDMS
ALU"! MIM-S'ILFATE
CATALYTIC OXIDATION OF SUL FUR-OIOXIDF. ADSORBED IN A SOLUTION
10/27/69
PAGE 11
AMMONIA
COMPOSITE FERTILI/ER FROM "HOSPHATE NITP.IC-ACID AMMONIA ANP
SULFUR-OIOXIDE NARIMNA7CFF
AMMONIA PROCESS FOR PF"OVAL OF SULFUR-OIOXIDE FP.CX FlUC GAS
NEWAHF APR
VISCOSITY AND INTERMOLF.CULAR POTENTIALS OF HVOROGHN'-SULF IDF
SULFWR-DIOXIDE AW 4M19NIA PAL AK67VIP
OXIDATION OF AMMONIA AMMONIA AND METHANE CARBCN-MONOXIOF
AND SULFUR-DIOXIDE RYLULRhOOOA
STUDY OF THE OXIDATION OF SULFUROUS-ANHYDP IDE AND AMMONIA
GAS IN THE PRESENCE HF PLATINUM AND RHODIUM
WF.NGP 18SOT
AMMONIA-OXIDATION
RECOVERY OF NOBLE METALS EVAPORATED FROM AMMONIA-OXIDATION
AMMONIACAL CATALYSTS HOLZH 65RON
OXIDATION OF AMMONIACAL SULFUR-DIOXI Of. SOLUTION WITH
OXYGEN IN A STIRRED AUTOCLAVE MAHABK64OAS
AMMONIUM
MANUFACTURING CONCENTRATED SULFUR-DIOXIDE FROM INDUSTRIAL
WASTE GASES BY THE AMMONIUM CYCLIC METHOD BETTJ 6SMCS
AMMONIUM-SULFAT E
A STUDY ON INDUSTRIAL PREPARATION OF AMMONIUM-SULFATF
BY NONCATALYTIC OXIDATION CHUNKY66SIP
SULFUR-DIOXIDE REMOVAL FROM GASES TO OBTAIN AMMONIUM-SULFATE
AMMONIUM-SULFITE GANZSN6«OR
UTILIZATION OF AMMONIUM-SULFITE SOLUTIONS FROM THE FINAL GAS
SCRUBBING SOLUTION OF THE CONTACT SULFUR1C-AC10
INSTALLATIONS CHEM 64UAS
AMMONIUM-SULFITE-BISULFITE
MASS TRANSFER COEFFICIENTS DURING THE ABSORPTION OF S02
FROM GASES BY AMMONIUM-SULFITE-BISULFITE SOLUTIONS
CHERBA64MTC
ABSORPTION OF SULFUR-DIOXIDE BY AMMONIUM-SULFITE-BISULFITE
SOLUTIONS IN A SPRAY TYPE VENTURI SCRUBBER VOLGBP66ASD
APPARATUS
CONTACT APPARATUS FOR THE OXIDATION OF SULFUR-DIOXIDE
APPARATUS FOR VAPOR-PHASE CATALYTIC REACTIONS * '"
BADG 64AFV
PROCESS AND APPARATUS FDR OXIDIZING SULFUR-DIOXIHE
DESIGNING OF CONTACT APPARATUS FOR THE OXIDATION OF' "
DIOXIDE RESKVS6SDOC
ABSORPTION OF SULFUR-TRIOX IDE IN A FOAM TYPE APPARATUS
HAVING AN INTERNAL FILM HEAT TRANSFER DEVICE
HLYAIGS6AST
NEW CONSTRUCTION MATERIALS FOR APPARATUS IN SULFUR IC-ACID
AND SELENIUM PRODUCTION BULYII62NCM
APPARATUS FOR EXOTHERMIC CATALYTIC REACTIONS CHRIA *8AEC
ELECTRIC DISCHARGE APPARATUS FOR THE SYNTHESIS OF
NITRIC-OXIDE FROM ATMOSPHERIC NITROGEN COT
AERODYNAMIC MODELLING OF CONTACT APPARATUS MODELLING
REACTOR FOR THE OXIDATION OF SULFUR-01 OXIDE TO
SULFUR-TRIOXIDE
COTTWJ«9EDA
- - OF A
EPMAA 68AMO
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10/27/69
APPARATUS
PAGE
12
APPARATUS FOR AFFECTING GAS REACTIONS BV MEANS OF ELECTRICAL
TFsflNG*OFETHE APPARATUS FOR THE OXIDATION OF CONCENTRAT ED*"*
SULFUR-DIOXIDE FILAVU66TOT
CATALYTIC APPARATUS SUITABLE FOR THE OXIDATION OF
SULFUR-DIOXIDE HECHI 26CAS
CATALYTIC CONVERSION APPARATUS SUITABLE FOR OXIDIZING
SULFUR-DIOXIDE HECHI 27CCA
APPARATUS AND PROCESS FDR CIRCULATING POWDERED SOLID IN
CHEMICAL TREATMENT-X HEMMCE52AAP
HEAT EXCHANGE APPARATUS FOR CATALYTIC EXOTHERMIC GAS-PHASE
REACTIONS SUCH AS OXIDATION OF SULFUR-DIOXIDE
HERMCV37HEA
CATALYTIC CONVERTER APPARATUS SUITABLE FOR OXIDIZING
SULFUR-DIOXIDE INGE 25CCA
CATALYTIC APPARATUS SUITABLE FOR CONVERSION OF
SULFUR-DIOXIDE TO SULFUR-TRIOXIDE
CATALYTIC APPARATUS
CATALYTIC APPARATUS FOR GAS REACTIONS .
METHOD AND APPARATUS FOR SUBDIVIDING PARTICULATE SOLIDS
JASPHP65MAS
APPARATUS FOR CATALYTIC OXIDATION OF GASES SUCH AS SULFUR-
DIOXIDE TO TRIOXIDE JEFFRC33AFC
APPARATUS FOR CONTACT OXIDATION OF SULFUR-DIOXIDE MITH A
FLUIDIZED-BEO OF CATALYST LABUGV59AFC
OXIDATION OF S02 IN AN APPARATUS WITH A FLUIDI ZED-BED OF FE-
OXIDE CATALYST DURING H2S04 PRODUCTION BY THE CONTACT
ISENH026CAS
JAEGAQ28CA
BCfl
JaCAF
PROCES
APPARATU
LASTYV6600S
FOR FAST DETERMINATION OF THE ACTIVITY OF
CATALYSTS FOR REACTIONS INVOLVING ABSORPTION OR EVOLUTION
OF HEAT MACAJ 67AFD
GAS ABSORPTION APPARATUS MELLRA66GAA
GAS AND LIQUID CONTACT APPARATUS MOORLP67GAL
APPARATUS FOR INTIMATE CONTACTING OF GAS WITH LIQUID
MORIJ 66AIC
NEW CONTACT APPARATUS FDR THE OXIDATION OF SULFUR-DIOXIDE IN
A FLUIDIZED CATALYST BED MUKHIP59NCA
APPARATUS FOR CATALYTIC SULFUR-DIOXIDE OXIDATION
PETEG 59AFC
CONTACT APPARATUS FDR OXIDIZING SULFUR-DIOXIDE
PETRNM67CAF
APPARATUS FOR INDICATING THE THERMAL EMF AND AC
CONDUCTIVITY OF A CATALYST RICHJT66AIT
LABORATORY APPARATUS FOR STUDYING CATALYTIC PROCESSES IN
FLUIDIZEO-BEDS RODED 68LAS
PERFORMANCE OF AN INDUSTRIAL APPARATUS FOR THE OXIDATION OF
S02 IN A FLUIDIZED CATALYST BED RIIMAES66POA
APPARATUS FOR CATALYTIC EXOTHERMIC REACTIONS IN THF GAS
PHASE SCHOR 67ACE
EXPERIENCE WITH OPERATION OF THE K-39-5 CONTACT APPARATUS
SHATNI66EOK
CONSTRUCTION MATERIALS FOR FILTERING APPARATUS IN
NICKEL COBALT PRODUCTION SHVAGL63CMF
10/27/69
APPARATUS
AQUEOUS
ARC-DISCHARGE
ARSENIC
ATMOSPHERE
ATMOSPHERES
PAGE
13
THE COMPUTATION OF CONTACT APPARATUS FOR THE OXIDATION OF
SULFUR-DIOXIDE ON AN APIABATIC CATALYST LAYER
SLINMG61TCO
GAS PURIFICATION PROCESS AND APPARATUS SDGR 66GPP
APPARATUS FOR CHEMICAL REACTIONS STFLP05ZAFC
LABORATORY APPARATUS WITH FLUI DI ZED-BED OF POWDERED CATALYST
SUVPAS64LAF
APPARATUS FOR TEMPERATURE CONTROL IN CATALYTIC REACTIONS
TAKEJ 54AFT
REASONS FOR THE RISE IN THE TEMPERATURE OF GASES IN FRONT
OF THE CONTACT APPARATUS OF AN INSTALLATION FOR PREPARING
SULFURIC-ACID BY WET CATALYSIS METHOD TSYGSA67RFT
APPARATUS FOR OXIDIZING SULFUR-DIOXIDE VARLML35AFO
METHOD AND APPARATUS FOR A FLUIDI ZED-BED REACTION
WAY DF66MAA
ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE AQUEOUS
SOLUTION FROM A GAS MIXTURE BLASH 66ASO
CATALYTIC OXIDATION OF SULFUR-DIOXIDE IN AQUEOUS SOLUTION
CHENCK52COO
THE REACTION OF SO? AND 02 IN AQUEOUS SOLUTIONS ON MNS04
COUGOR6'
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10/77/69
ATMOSPHERIC
PAGE
ELECTRIC DISCHARGE APPARATUS FOR THE SYNTHESIS OF
NITRIC-OXIDE FROM ATMOSPHERIC NITROGEN COTTWJ49EOA
MODERN TECHNIQUES OF STUDY OF CORROSION AND ATMOSPHERIC
PQLLUTinN APPLIED TO BOILERS AND FURNACES ETOCP 66MTS
EFFECT OF SULFUR-DIOXIDE ON THE ATMOSPHERIC CORROSION OF
MILD STEELS
UG
CATALYTIC PROPERTIES OF FERRIC-HYDROXIDE IN THE OXIDATION OF
SUGAH 65ESO
SULFUR-DIOXIDE BY ATMOSPHERIC OXYGEN
BARIUM-ALUM! NIIM-VANAOATE
TALIM 37CPO
INFLUENCE OF CATALYSIS CONDITIONS ON CONTENT OF SULFUR IN
BARIUM-ALUMINUM-VANAOATE CATALYST DURING THE OXIDATION OF
SULFUR-DIOXIDE KORNGP56IOC
BARIUM-ALUMINUM-VANADIUM
EFFECT OF TRANSPORT ON THE KINETICS OF OXIDATION OF
SULFUR-DIOXIDE ON A BARIUM-ALUMINUM-VANADIUM CATALYST
INVESTIGATION BY THE DIAPHRAM METHOD ROITVAS8EOT
KINETICS OF THE CATALYTIC FORMATION OF SULFURIC-ACID ON A
BARIUM-ALUMINUM-VANADIUM CATALYSTS RZAEPB60KOT
BAUR'S
BAYER
BED
THE NATURE OF BAUR'S KINETICS
BAURE 44TNO
THE BAYER DOUBLE-CONTACT PROCESS FOR CONVERTING S02 TO S03
UCQTU 6&TRD
THE BAYER DUAL CATALYST PROCESS WERTH 65TBD
CALCXJLAIIONS FOR FLUIDIZED BED CATALYTIC EQUIPMENT
PURIFICATION OF SULFURDUS RESIDUAL GASES BY ALUMINA BE065C
AZOUA 64PSP
GRADED SUPPORT BED FOR CATALYSTS CHRICM65GSB
CATALYTIC OXIDATION OF SULFUR-DIOXIDE GAS IN A FLUIOIZED BED
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSI5°?I?LTHECO°
EFFECT OF CATALYST CONDUCTIVITY ON THE APPARENT
CONDUCTIVITY OF THE CATALYST BED AND THE HEAT TRANSFER
COEFFICIENT FROM THE BED TO REACTOR BATH HORAJ 67HAM
FLUIDIZED BED PROCESSES
JAVOJ 66FBP
OXIDATION OF S02 IN A FLUIDIZED CATALYST BED KERNVS6600S
LIMITING CONDITIONS OF THE EXISTENCE OF A GRANULAR
TH
CATALYST BED KURGVM65TLC
KINETICS OF SORPTION AND OF THE CHEMICAL REACTION ON A
UNIFORM-SURFACE CATALYST IN A FLUIDIZED BED INVOLVING
COMPLETE INTERMIXING OF PARTICLES AND OF THE GAS
OPTIMAL ADIABATIC BED REACTORS FOR SULFUR-DIOXIDE WITH COLO
NEW CONTi
APPARATUS FDR THE OXIDATION OF SULFUR-DIOXIDE IN
A FLUIDIZED CATALYST RED MUKHIP59NCA
THE USE OF CONTACT EQUIPMENT WITH A FLUIDIZEO CATALYST BED
IN THE MANUFACTURING (IF SULFUR IC-ACID MUKHIP63TUO
PERFORMANCE OF AN INDUSTRIAL APPARATUS FOR THE OXIDATION OF
S02 IN A FLUIDIZED CATALYST RED
OXIDATION OF SULFUR-DIOXIDE IN
CATALYST
RUMAES66POA
A FLUIDIZED BED WITH VANADIUM
SZOLP 5500S
1*9
10/27/69
PAGE
15
RED
BtDS
BENCH-SCALE
BIBLIOGRAPHY
BOROPHOSPHATE
ROUNDRY
BOYLE-CURVES
OVERALL RATE OF CATALYTIC REACTIONS AS INFLUENCED BY THE
INHOMOGENEITY OF THE FLUIDIZED RED TODEOM660RO
KINETICS OF THE OXIDATION OF S02 IN A FLUIDIZED CATALYST BED
TRABDG59KOT
FPOMGF66HAM
LEWIK 49HRF
ISTRIBUTION
HEAT AND MASS TRANSFER IN CATALYT1C,BEDS
HEAT REMOVAL FROM FLUIDIZED SOLID REACTOR BEDS
HEAT TRANSFER IN GRANULAR BEOS TEMPERATIIR DIS
IN THE CATALYST BEOS FOR SULFUR-DIOXIDE OXIDATION
MfltDS 5 IH T I
BENCH-SCALE INVESTIGATIONS ON REMOVING SULFUR-DIOXIDE
FROM FLUE GASES RIEND 60BSI
SULFUR-OXIDES AND OTHER SULFUR COMPOUNDS A BIBLIOGRAPHY WlTH
ABSTRACTS GROSA &SSOA
ABRASION RESISTANT GRANULATED BOROPHOSPHATE
RAOEJ 67ARG
NUMERICAL SOLUTION OF TWO-POINT BOUNDRY VALUE PROBLEM VALUE
PROBLEMS IN SIMULTANEOUS SECOND-ORDER NONLI NEAR. OP.DI NARY
DIFFERENTIAL
>IMULTAN
EOUATIO
NS
LIU SL67NSH
CALCIUM-CHLORIDE^^^
USE OF THERMODYNAMIC SIMILARITY FOR THE DETERMINATION OF
BOYLE-CURVES OF SUBSTANCES STUDIED IN A LIMITED
TEMPERATURE INTERVAL KAZAYZ66UTS
CALCIUM-CHLORIDE WITH SULFUR-TP IOX I DE
SUG I K onPCC
ABSORPTION OF SULFUR-DIOXIDE BY CALCIUM-HYDROXIDE SLURRY
MISAY 67ASO
CALCULATING
CALCULATION
THE LAW OF MASS-ACTION AS THE BASIS FOR CALCULATING THF BEST
YIELD FROM TECHNICAL . AND ECONOMIC STANDPOINTS SftvEH 52TLn
NOMOGRAMS FOR CALCULATING THE PERCENTAGE OF SULFUR-DIOXIDE
CONVERTED INTO SULFUR-TR FOXIDE AND THE COMPOSITION OF
OLEUM SHRASS36NCP
CALCULATION OF THE RATE OF REACTION CONSTANTS IN THE
OXIDATION OF S02 TO S03 ON A VANADIUM CATALYST „„„.,,,.„
RU" YK Ao 3C n i
ALLOWANCE FOR THE TEMPERATURE DEPENDENCE OF SPECIFIC HEAT
OF INDIVIDUAL GASES AND GAS MIXTURES IN THERMOOYNAMIC
CALCULATION FOR GAS FLOW MACHINE FISCS 6JATn
CALCULATION OF THE OVERHEATING OF CATALYST PARTICLES IN THE
OXIDATION OF SULFUR-DIOXIDE GABRC047COT
CALCULATION OF THE RATE OF A HALF ORDER REACTION PROCEEDING
IN PORES OF A CATALYST C.LASV IShCOT
CALCULATION OF THE FLUIDI ZED-BED CATALYTIC PROCESS ,„.„._„
KF RNVSo 3C Fr
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10/27/69
CALCULATION
CALCULATIONS
CALOERBANK
CAPACITY
CARBON
PACE
16
CALCULATION OF THF OPTIMAL CONDITIONS FOR CHEMICAL REACTORS
OF THE COMBINED TYPE KINGRP65COT
CALCULATION OF HEAT TRANSFER COEFFICIENTS IN TUBULAR
CATALYTIC REACTORS SADOAS65COH
CALCULATION OF THE SULFUR-TRIOXIOE CATALYSIS SCHW 52COT
SOME OBSERVATIONS ON THE CALCULATION OF HETEROGENEOUS
CATALYSIS VANDC 62SOO
CALCULATIONS FOR FLUIDIZED BED CATALYTIC EQUIPMENT
ANOK 65CFF
MATERIAL AND HEATING BALANCE CALCULATIONS IN CHEMICAL
TECHNOLOGY GELEH 66MAH
DESIGN CALCULATIONS FOR PROCESSES IN FIXED-BEDS AND
FLUIDIZED-BEOS OF CATALYST KUZIVA650CF
MECHANISM OF THE CATALYTIC OXIDATION OF SO2 CONSIDERED
FROM THE THEORY OF SEMICONDUCTOR CORRECTION OF THE
MECHANISM OF CALDERBANK KAWAT S«TPP
IMPROVED CATALYST OF HIGH LOAD CAPACITY FOP SULFURIC-ACID
PRODUCTION BUDA 66ICO
APPLIED HYDROCARBON THERMODYNAMICS HEAT CAPACITY DIFFERENCES
EFFECT OF TEMPERATURE ON THE RATE OF FORMATION OF SULFURIC
BY THE OXIDATION OF SULFUR-DIOXIDE ON ACTIVATED CARBON BY
THE LIQUID CONTACT METHOD DAVTOK61ETR
INVESTIGATION OF THE MECHANISM OF OXIDATION HYDROGENATION
AND ELECTROCHEMICAL COMBUSTION ON SOLID CATALYST
ACTIVATED CARBON AT 20-DEG
OAVTOK61IMO
OXIDATION OF SULFUR DIOXIDE ON
IN THE PRESENCE OF WATER VAPOR
THE MECHANISMS OF OXIDATION HYDROGENATION AND
ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS RELATION
BETWEEN DEPOLARIZING OXIDES ADSORBED ON CARBON AND
PLATINUM AND THE CATALYTIC ACTIVITY IN THE OXIDATION OF
SULFUR-DIOXIDE • OAVTOK61TMO
FLOW OF SULFUR-DIOXIDE OVER THE SURFACE OF SPHERON-6(27001
GRAPHITIZED CARBON SLACK POPECG67FSD
THE MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE INFLUENCE OF TEMPERATURE AND TIME OF CARBON
OESORPTION ON ADSORPTION AND OXIDATION OF H2S AND S02
SIF.OJ 64MCO
REMOVAL OF S02 FROM GASES BY USING VARIOUS GRADES OF
ACTIVATED CARBON SIEDJ 64RSG
DETERMINATION OF THE NUMBER OF ACTIVE CENTERS ON THE CARBON
SURFACE BY THE ELECTROCHEMICAL METHOD IN OXYGEN
CHEMISORPTION SIEDJ 6SDNA
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE CONTRIBUTION OF CARBON FREF-RADICALS IN THE
S02 TO S03 OXIDATION PROCESS SIEDJ 6SMCD
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THF. CONCENTRATI (IN OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND S02 OXIDATION
PROCESSES SIEDJ 66MCO
51
11/27/69
CARBON-BLACK
CARHON-OinxIDE
CARBON-MONOXIDE
PAC>F
17
CARBON-TYPE
CARBONS
CARRIER
(.APPIERS
CONTAMINATION OF A VANADIUM CATALYST WITH CARBON-BLACK IN
SULFURIC-ACID PRODUCTION BURYKA63COA
THE FFFECT OF CARBON-MONOXIDC AND CARRON-OI OX IDF ON THF
CQURSF. OF THE CONTACT OXIDATION OF S'Jl FUR-01 OX (OK Tfl
S'JLHUK-TRIOXIDfc YAKir«34Trr
"INFLUENCE OF CARBON-MONOXIDE ON THE ACTIVITY OF PLATINUM
CATALYSTS DURING THF OXIDATION OF SULFIIR-DI 0X1 DF: Tr>
SULFUR-TRIOXIDE fc PF KVY'IHI nr.
THERMODYNAMIC CONSIDERATION ON THE CATALYTIC OXIDATIHN OF
CARBON-MONOXIDE AND SULFUR-DIOXIDE SFIY1 61TCO
REMOVAL OF CARBON-MONOXIDE AND SULFUR-ACIDS FROM FLUE-GASES
TILHP ^jfiRf.M
EFFECT OF VANADIUM PENTOXIDE ON GAS-PHASE COMBUSTION I THE
CARBON-MONOXIDE SULFUR-DIOXIDE OXYGEN SYSTEM
CATALYTIC PROPERTY OF VANADIUM-OXIDE IN THE REOUCTIOr, OF-
SULFUROUS GAS BY CARBON-MONOXIDE VISCYS«5C"n
THF EFFECT OF CARBON-MONOXIDE AND CARBON-DIOXIDE IN THE
COURSE OF THE CONTACT OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE YAKIEM34TEO
CARBON-TYPE CATALYST FOR THE CONVERSION OF SULFUR-DIOXIDE
TO SULFUR-TRIOXIDE META 64CTC
THE CHEMISORPTION OF SULFUR-DIOXIDE ON CARBONS
BILLBH66CSD
THE USE OF FE304 BY-PRODUCTS FROM BETA-NAPTHYLAMINE
PLATINUM CARRIER IN THE CONTACT OXIDATION OF -—
AS A
SO?
ADAniE36TI|0
BALL-SHAPED CATALYST OR CARRIER APAMM 6»,BSC
DISTRIBUTION OF NOBLE-MFTALS ON CARRIER CATALYSTS
KRALH ftSDNM
CARRIER CATALYSTS RIENG 6'.CC
INVERS MIXED CATALYSTS SULFUR-TRIOXIDE SYNTHESIS USING
IRON-OXIDE CATALYST ON A SILVF.R CARRIER SCHWGMfcTlMC
REGENERATION AND REACTIVATION OF DEACTIVATED PLATINUM
CATALYST ON A CARRIER SHEl A2RAR
THE INFLUENCE OF THE CARRIER ON THF. ACTIVITY OF THE VANADIUM
CATALYSTS FOR THF OXIDATION OF SULFUROiJS-ftNHYORinf
COMPARATIVE CATALYTIC ACTIVITY OF CENTERS flN THE SURFACe OF
CRYSTALS AND OF AN INERT CARRIER STRr£V64CC»
VANADIUM CATALYST USED IN THE OXIDATIUN OF SO? EFFFCT OF
MECHANICAL TREATMENT PF CARRIER ON THE ACTIVITY OF CONTACT
SUINA
UTILIZING WASTE FROM THF ALUMI NUM-CHLOR I OF INDUSTRY t-na
CARRIERS OF PLATINUM IN THF OXIDATION C\f SULFUR-PI nx I nr Tr
SULFUR-TRIOXIOE APADI FlMIWf
EFFECTS OF CARRIERS AND DILUENT ON THE ENFRGY OF ACTIVATWN
AND THE VALUE OF THE DISPERSION COEFFICIENT
AnADIE36ECD
52
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IC/27/69
CARRIERS
PAGE 18
CEMENTS
CFftAMIC
CHAMBER
PREPARING CORUNDUM CARRIERS FOR CATALYSTS GPIGAFbBPCC
REGULATION OF POROSITY AND MECHANICAL STRENGTH OF SHAPED
KIESELGUHR CATALYST CARRIERS JELUF65RPM
SURFACE STRUCTURE OF KIESELGUHR CARRIERS AND CATALYSTS FOR
THE OXIDATION DF SULFUR-DIOXIDE JIRUP 5TSSO
THE INFLUENCE OF CARRIERS ON THE CATALYTIC PROPERTIES OF
VANADIUM-PENTOXIDE KARMM034TIO
THF. INFLUENCE OF CARRIERS ON THE CATALYTIC PROPERTIES OF
VANADIUM-PENTOX10E KHAROM34TIO
MACROPOROUS CATALYST CARRIERS OF SILICA-GEL OR
ALUMINUM-SILICATE SALTVP60MCC
EFFECT OF CARRIERS ON THE ACTIVITIES AND PROPERTIES OF
VANADIUM CATALYSTS FOR THE OXIDATION OF SULFUR-TRIOXIDE
SOLOBI64EOC
PREPARATION OF CORUNDUM CARRIERS FOR CATALYSTS
A STUDY OF ADSORPTION ISOTHERMS ON OXIDE FORMS OF"
METALSILICATE CARRIERS AND CATALYSTS
RESISTANCE TO ACIDS OF AUTOCLAVEO CEMENTS
POROUS CERAMIC BALLS FOR CARRYING CATALYSTS
CERAMIC CATALYST HAVING A FLAME SPRAYED COATING
PLATINUM FAMILY METAL
USE OF AN IRON CATALYST IN
ZLATSGbbPCC
ZULFZG66SAI
NURMSM66RAA
FISCHCt«CB
OF A
TEAGED64CCH
CHAMBER-PROCESS
THE CONTACT CHAMBER PROCESS
ESELIM64UOA
THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE A STUDY OF THE
CATALYST CHAMBER SALSF S2TCO
CATALYTIC OXIDATION OF SULFUR-DIOXIDE AS A FUNCTION OF
RESIDENCE TIME OF THE GASES IN THE REACTION CHAMBER
HICKK 61COO
THEORY OF THE CHAMBER-PROCESS MECHANISM AND THE
CHARACTERIZATION
STRUCTURAL CHARACTERIZATION OF CATALYSTS
OF MERCURY
STRUCTURAL CHARACTERIZATION OF CATALYSTS
OF DATA ON GAS ABSORPTION
CHARCOAL
CHARCOALS
CHEMISORPTION
KINETICS OF
KUZMIN3bTOT
PORROSIMMETRY
ASENJ 67SCC
INTERPRETATION
ASENJ 67SCP
THE CONTACT EFFECT OF CHARCOAL IN QxIOATIVF REACTIONS
OOROAG17CEC
OXIDATION OF SULFUR-DIOXIDE ON ACTIVATED CHARCOAL BY LIQUID
CONTACT METHOD OVCHEN560SD
GAS-ABSORBING CHARCOALS RFINLU66GAC
THE CHEMISORPTION OF SULFUR-DIOXIDE ON CARBONS
RILLBH66CS
CHEMISORPTION AND MECHANISM OF CATALYTIC REACTION'S ON OXIDE
CATALYSTS KPAUA 62CAM
CHEMISORPTION nESORPTHIN AND MECHANISMS OF CATALYTIC
REACTIONS ON METAL CATALYSTS KRAUA 63COA
53
10/27/69
CHEMISORPTION
CHLORINE
PAGE \«
A PERTURBATION CHROMATOGRAPHIC INVESTIGATION OF
CHEMISORPTION AND CHEMICAL REACTION ON A SOLID CATALYST
DETERMINATION OF THE NUMBER OF ACTIVE CENTERS ON THE CARBON
SURFACE BY THE ELECTROCHEMICAL METHOD IN OXYGEN
CHEMISORPTION SIEOJ 650NA
CHROMATOGRAPHIC
STUDY OF CORROSION OF
SULFUR-DIOXIDE BY ~
IRON AND ITS ALLOYS IN CHLORINE AND
THE THERMOGRAPHIC METHOD -~ "
TOVMK66SCI
A PERTURBATION CHROMATOGRAPHIC INVESTIGATION OF
CHEMISORPTION AND CHEMICAL REACTION ON A SOLID CATALYST
SGS '
CHROME
CHROMIC
CHROMIUM
DIFFERENTIAL CHROMATOGRAPHIC METHOD OF STUDYING THE
KINETICS OF CATALYTIC REACTIONS
MUSSGS66PCI
CHROME CATALYSTS FOR THE CATALYTIC OXIDATION OF
SULFUR-DIOXIDE
CHROMIC CATALYSTS SUPPORTED ON AL203
ROGISZ67DCM
AOAOIE3nCAF
KUEZH 67CCS
INFLUENCE OF THE COMPOSITION AND THE DISTRIBUTION OF THE
CATALYTIC MASS ON THE ACTIVITY OF CHROMIUM CATALYSTS
THE POISONING OF CHROMIUM CATALYSTS BY ARSENIC AND^OTHER*
CONTACT POISONS ADADIE35TPO
THE EFFECT OF METAL OXIDE ADMIXTURES ON THE ACTIVITY OF THE
TIN CHROMIUM CATALYST GERNDV35TEO
EFFECT OF HYDROGEN-SULF IDE AND SULFUR-DIOXIDE ON THE
CORROSION OF CHEMICALLY RESISTANT CHROMIUM NICKEL STEEL
IN A SODIUM-SULFATE SOLUTION ACIDIFIED WITH SULFURIC-ACI0
HERBG bftEHS
EFFECT OF HIGH TEMPERATURE PLASTIC DEFORMATION AND
SUBSEQUENT QUENCHING ON THE CORROSION AND MECHANICAL
PROPERTIES OF CHROMIUM NICKEL AUSTENTIC STEELS
TAVALF67EHT
CHROMIUM-ALUMINA
• OXIDATION OF SULFUR-DIOXIDE ON NON MODIFIED CHROMIUM-ALUMINA
CATALYSTS KUEZW &SDOS
CHROMIUM-NICKEL-MOLYBOENUM-COPPER
CORROSION BEHAVIOR OF CHROMIUM-NICKEL-MOLVBDENUM-COPPER
STEELS IN SULFUR 1C AND EXTRACTION PHOSPHORIC-ACIDS
SIDOYS67CBC
CHROMIUM-OX IOE
CHROM IUM-GX IDE-ST ANN IC-OX f
CONTACT PRO
CONTACT PROPERTIES OF CHROMIUM-OXIDE IN THE OXIDATION
OF SULFUR-DIOXIDE TO TRIOXIOE . ADADIE38CPC
THE ACTIVITY OF CHROMIUM-OXIDE STANNIC-OXIDE CATALYSTS FOR
THE OXIDATION OF S02 TO S03 KU"MNP56ACP
CONTACT PROPERTIES OF CHROMIUM-OXIDE IN THE OXIDATION OF
SULFUR-DIOXIDE PPSTVF3fiCPO
" ~" DE
PERTIES OF CHROMIUM-OXIDE-STANNIC-OXIDE CATALYSTS
FOR THE OXIDATION OF S02 TO SD.1
KURINP56CFP
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10/27/69
PAGE 2C
CHROMIUM-VANADIUM CATALYST WITH A HIGH VELOCITY CONSTANT
CLAY
cn
COAL
COLUMBIUM
COMPRESSORS
COMPUTER
COMPUTERS
CONDUCTIVITY
CONSTRUCTION
55
COLLOIDAL CLAY AS CATALYST
AOAOIE3TCVC
IN OXIDATION AND HYDROGENATION
HAY JG20CC<
STABLE AND UNSTABLE BEHAVIOR OF ADIABATIC TUBULAR REACTOR
AS FOR EXAMPLE IN CATALYTIC CO OXIDATION PADBG 67SAI
HXIOATION OF S02 IN AIR AT 950-DEGREES COOPERATIVE
INFLUENCE OF CO AND NO SHAHJTbbOOS
RECOVERY OF SULFUR-DIOXIDE FROM COAL COMBUSTION STACK .^
HEINIB RSC
METHODS OF REDUCING EMISSION OF OXIDES OF SULFUR FROM COAL
" -1 •" - ' PERRH 65MOf
SULFUR-DIOXIDE AND FLY ASH REMOVAL FROM COAL BURNING
POWER PLANT POLLWA67SDF
METHODS OF REDUCING EMISSIONS OF OXIDES OF SULFUR FROM COAL
U.S.DE65HRE
COLUM81UM AND TANTALUM-OXIDES IN THE CONTACT PROCESS
PLATMS37Cm
COMPRESSORS WITH HYDRAULIC PISTONS FOR CORROSIVE GASES
TETEVI67CWY
COMPUTER PROGRAM-FOR AN ADIARATIC CATALYTIC REACTOR
CHAMJP66CPF
COMPUTER PROGRAM FOR AN ADIABATIC CATALYTIC REACTOR
HANOJP66CP/
ALGEBRAIC MANIPULATIONS OF THE RATE EQUATIONS OF CERTAIN
CATALYTIC REACTIONS WITH A DIGITAL COMPUTER
OPTIMUM CONTROL OF SULFURIC-AC ID PRODUCTION WITH THE AID _,
OF COMPUTERS GAFUAA6SOCC
THERMAL CONDUCTIVITY OF SULFUR-DIOXIDE AND OIETHYL-ETHER
AT DIFFERENT TEMPERATURES
.... __ - HETEROGENEOUS CATALYSIS
EFFECT OF CATALYST CONDUCTIVITY ~ ~ "
UPTAD6TTCS
II. THE
CONDUCTIVITY OF THE CATALYS
COEFFICIENT FROM THE "- —
HEAT AND MASS TRANSFER IN ...
ON THE APPARENT
Sf BED AND THE HEAT TRANSFER
_ BED TO REACTOR BATH HORAJ 67HAJ
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS VII EFFEC1
OF CATALYST HEAT CONDUCTIVITY ON THE OVERALL HEAT
TRANSFER COEFFICIENT IN A PACKED TUBE MANUP 67HA»
APPARATUS FOR INDICATING THE THERMAL EMF AND AC
CONDUCTIVITY OF A CATALYST
CHANGES IN THE CONDUCTIVITY AND WORK-ruNCTI ON OF
ELECTRON UPON ABSORPTION OF 0 AND S02 AND V205
RICHJT66AIT
THE
LAYERS
SURNf
NEW CONSTRUCTION MATERIALS FOR APPARATUS
AND SELENIUM PRODUCTION
ILN65C11
IN SULFURIC-AC1D
BULVI162NC*
10/27/69
CONSTRUCTION
CONTACT
PAGF
21
SELECTION OF CATALYSTS AND CONSTRUCTION OF CATALYTIC SYSTFMS
CONSTRUCTION MATERIALS FOR FILTERING APPARATUS , NRC1G ' SZ*ASOC
NICKEL COBALT PRODUCTION SHVAGL53CMF
CONTACT REACTION RATE OF S02 OXIDATION UNDER PRESSURE
ABE K 6HCRR
THE POISONING OF CHROMIUM CATALYSTS BY ARSENIC AND OTHER
CONTACT POISONS ADAOIE35TPO
THE USE OF FE304 BY-PRODUCTS FROM BETA-NAPTHYL AMINE AS A
PLATINUM CARRIER IN THE CONTACT OXIDATION OF S02
AOADIF36TUO
ACTION OF HYDROGEN-FLOUR IDE ON THE VANADIUM-BARIUM CONTACT
MASS FOR THE OXIDATION OF S02 ADAOIE37AOH
CONTACT PROPERTIES OF CHROMIUM-OXIDE IN THE OXIDATION
OF SULFUR-DIOXIDE TO TRIOXIDE ADADIESSCPf
CONTACT OF FLUIDIZABLE SOLIDS WITH GASEOUS FLUIDS
TUBULAR HEAT EXCHANGER
SULFURIC-ACID PLANTS
RECOVERY OF VANADIUM FROM
CONTACT APPARATUS FOR THE OXIDATION OF SULFUR-C
FOR THE CONTACT UNITS nF"««SP««*F
AFANPA38THE
_. _.. THE CATALYST USED IN THE CONTACT
ACID PROCESS ALBEFM64ROV
OPTIMIZATION OF THE PROCESS OF SULFURIC-ACID PRODUCTION BY
THE CONTACT METHOD AMELAG6600R
IMPROVED QUALITY OF CONTACT OF SULFURIC-ACID APAKiA65ioc
PREVENTING THE FORMATION OF SULFURIC-ACID FOG IN THF CONTACT
PROCESS FOR SULFUR IC-ACIO MANUFACTURE APAK I Af-ISPFS
EXPERIMENTAL REACTORS FOR CONTACT CATALYSIS RAKOHM65EBC
PMENT OF CONTACT --.- —
:T CATALYTIC RFACTORS
HAKHM fc7OCC
DEVELOPMENT OF CON ... ._
DESIGN OF CONTACT PROCESS EQUIPMENT WITH AN ADIASATIC
CATALYST LAYER FOR THE OXIDATION OF SUIFUR-OI OXt OE DESIGN
OF EQUIPMENT WITH THE INTRODUCTION OF COLD REACTION
MIXTURES AND WITH INTERMEDIATE HEAT EXCHANGERS
DETERMINATION OF THE STATIC CHARACTERISTICS OF A CONTACT™00
REACTOR FOR THE OXIDATION OF SULFUR-DIOXIDE WITH THE AIM
OF OPTIMIZING THE PROCESS KFSKVS&4OOT
DESIGNING OF CONTACT APPARATUS FOR THE OXIDATION OF
DIOXIDE BESKVS6*OQC
SELECTION OF MATERIAL FOR CONTACT CATALYSTS BEHAVIOR AND
OF SEMICONDUCTING CATALYSTS BLOCJ 56SOM
OF THE CONTACT OXIDATION OF SULFUR-OIPX IDF
BOREGK31TKP
.ONCENTRATION OF SULFU"-OI 0X1DE IN CONTACT
:ID PRODUCTION ir.RFGKJ 7Tnf.
ONTACT OXIDATION OF SULFUR-DIOXIDE IN THE
_; FERRIC-OXIOE HOP.FGK44KOC
KINETICS OF THE CONTACT SYNTHESIS r\f SULFURIC-AC 10
PROPERTIES
THE KINETICS
THE OPTIMUM C
SULFURIC-AC
KINETICS OF C
PRESENCE 0-
SU1FUR-TRIOXIDE PRODUCTION WITH OXYGEN BY THF. CONTACT"MF THOP
BOREGK47STP
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10/27/69
CONTACT
57
PAGE 22
CONTACT SULFURIC-ACIO DETERMINATION OF WATER FORMED ON
THE CATALYST BROOM 48CSA
CONTACT PROCESS CONVERTER DESIGN CALDPH53CPC
STUDIES OF THE RATE OF REACTION IN THE VANADIUM CONTACT
SULFURIC-ACIO PROCESS
CHANHY36SOT
UTILIZATION OF AMMONIUM-SULFITE SOLUTIONS FROM THE FINAL GAS
SCRUBBING SOLUTION OF THE CONTACT SULFURIC-ACIO
INSTALLATIONS CHEM 64UAS
UTILIZATION OF SOLUTIONS OBTAINED BY NH3 SCRUBBING OF GASES
FROM CONTACT SULFURIC-ACIO INSTALLATION CHEM 6SUOS
CATALYTIC PROCESS FOR THE MANUFACTURE OF SULFURIC-ACIO IN
SEVERAL CONTACT AND ABSORPTION STEPS CHEM 66CPF
AUTOMATION OF CONTACT REACTORS IN THE CHEMICAL INDUSTRY
PRODUCTION OF SULFURIC-ACID BY THE CONTACT PROCESS
CIMAJ 67POS
ON THE RATE OF FORMATION OF SULFUR1C
EFFECT OF TEMPERATURE
BY THE OXIDATION OF
THE LIQUID CONTACT M
THE CONTACT EFFECT OF CHARCOAL IN OXIOATIVE
SULFUR-DIOXIDE ON ACTIVATED CARBON BY
ETHOO DAVTOK61ETR
--------- -------------- REACTIONS
DOROAG17CEC
AERODYNAMIC MODELLING OF CONTACT APPARATUS MODELLING OF A
TO
OF AC TOR FOR THE OXIDATION OF SULFUR-DIOXIDE
US
ULFUR-TRIOXIDE
OF AN IRON CATALYST
6BAMO
ERMAA
IN THE CONTACT CHAMBER PROCESS
CONTACT MASSES FOR HETEROGENEOUS GAS CATALYSIS E LIM6*UOA
THE CONTACT OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TR?OXIDEW
GISTAH37TCO
DETERMINATION OF
HARAH SBCRR
MEASUREMENT OF
HARAH 59CRM
APPLICATION OF THE
UNDER PRESSURE
CONTACT REACTION RATE OF S02 OXIDATION
THE RATE BY A DIFFERENTIAL METHOD
CONTACT REACTION RATE OF S02 OXIDATION
THE RATE OF FOUR DIFFERENT FEED GASES
CONTACT REACTION RATE OF S02 OXIDATION ... _. .
RATE EXPRESSION TO NEW OBSERVATIONS AND ILLUSTRATION FOR
THE CONVERTER DESIGN . HARAH 59CRR
SULFURIC-ACID OPTIMIZED CONDITION IN CONTACT MANUFACTURE
HOMMAC61SAO
THE DOUBLE CONTACT PROCESS OF SULFURIC-ACID MANUFACTURE
KAMIY 67DCP
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SULFIDE ON
COMPLEX SPIRALS OF PLATINIZED NICHROHE KOTENZ57COO
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYOROGEN-SULFIDE
ON COMPLEX SPIRALS OF PLATINIZED NICHROHE KOTENZ57COS
CONTACT CATALYST FOR SULFUR-DIOXIDE OXIDATION
t-UR THE OXIDATION OF S02 TO SO3
APPARATUS FOB CONTACT OXIDATION OF
FLUIDIZEO-BEO OF CATALYST
?*Q?.E?TiES..OF CHROMIUM-OXlDE-STANNIC-OXlDE
KUCZWJICCF
SULFURIC-ACIO BY CONTACT PROCESS
OXIDATION OF S02 IN AN APPARATUS
KURINP56CFO
SULFUR-DIOXIDE WITH A
LA8UGV59AFC
LAMMC 66SAC
WITH A FLUID!ZED-BED OF FE-
OXIOE CATALYST DURING H2S04 PRnnilCTION BY THE CONTACT
PROCESS LASTYV6600S
10/27/69
CONTACT
PAGE
23
rLUCPue ur HE
CONTACT SULFl
NVERSION STAC
CONTACT PROCE
CONV
INFLUENCE OF REACTION RATE ON OPERATING CONDITIONS IN THE
—LFURIC-ACIO MANUFACTURE LEWIWK25IOR
^GE IN THE MANUFACTURE OF SULFURIC-ACID BY
. .._CESS LOWRGC5BCSI
CONTACT OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIDXIDE UNDER
PRESSURE LUKYPM33COO
OPTIMUM SHAPES AND SIZES OF ELEMENTS OF A VANADIUM CATALYST
FOR THE PRODUCTION OF CONTACT H2S04 MALKV1640SA
PRODUCTION OF SULFUR-TRIOXIDE BY THE CONTACT PROCESS
MfTA 52POS
HEATING AND COOLING OF SULFURIC-ACID CONTACT CONVERTERS
MET A 66HAC
GAS AND LIQUID CONTACT APPARATUS MOORLP67GAL
NEW CONTACT APPARATUS FOR THE OXIDATION OF SULFUR-DIOXIDE IN
A FLUIDIZED CATALYST BED HUKHIPS9NCA
THE USE OF CONTACT EQUIPMENT WITH A FLUIOIZEd CATALYST BED
IN THE MANUFACTURING OF SULFURIC-ACIO HUKHI P
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10/27/69
CONTACT
CONVERSION
CONVERTER
PAGE
THE EFFECT OF CARBON-MONOX IDE AND CARBON-DIOXIDE ON THE
COURSE OF THE CONTACT OXIDATION OF SULFUR-DIOXIDE TO
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10/27/69
CORROSION
CORROSIONS
CORROSIVE
CORUNDUM
COTTON
CRACK INO
CRYSTAL
CRYSTALLINE
CRYSTALS
CYLINDRICAL
DEACTIVATED
El
PAGE
EFFECT OF SULFUR-DIOXIDE ON THE ATMOSPHERIC CORROSION OF
MILD STEELS SUGAH 65ESD
THE RELATION BETWEEN ACCELERATED CORROSION TESTS AND
OUTDOOR EXPOSURE ~~ " ~
THE
TESTS OF ELECTROPLATED COATINGS
SUGAS 65RBA
RELATION BETWEEN
_KPOSURE TESTS OF .
EFFECT OF HIGH TEMPERATURE PLASTIC DEFORMATION AND
ACCELERATED CORROSION TESTS AND OUTDOOR
ELECTROPLATED COATINGS SUGAS 65RBC
_ ATURE PLASTIC DEFORMATION AND
SUBSEQUENT QUENCHING ON THE CORROSION AND MECHANICAL-
PROPERTIES OF CHROMIUM NICKEL AUSTENTIC STEELS
EFFECT OF SILICON ADDITIONS ON THE CORROSION BEHAVIOR OF
HIGH-ALLOY AUSTENTIC STEEL IN SULFURIC-ACID SOLUTIONS
STUDY OF CORROSION OF IRON AND ITS ALLOYS IN CHLORINE AND
SULFUR-DIOXIDE-BY THE THERMOGRAPH 1C METHOD TOVMIK66SCI
TYPES OF CORROSION AND BEHAVIOR OF METALS AND ADDITIVES IN
BOILER FURNACES HICKK 65TCB
PROBLEMS OF CORROSIONS AND DEPOSITS ON THE FLUE-GAS SIDE
OF HEATING SYSTEMS 8ERGP 57PCO
BEHAVIOR OF TOMBAC ALLOY IN SOME CORROSIVE MEDIA
MERMS 66BTA
COMPRESSORS WITH HYDRAULIC PISTONS FOR CORROSIVE GASES
TETEVI67CWY
PREPARING CORUNDUM CARRIERS FOR CATALYSTS
PREPARATION OF CORUNDUM CARRIERS FOR CATALYSTS
OXIDATION OF S02 BY
SILICA —
COTTON
CRACKING CATALYSTS
GRIGAF6BPCC
ZLATSG66PCC
._ ..._.. _ .__ 02 OR 02-03 MIXTURE IN THE PRESENCE OF
SILICA-GEL ADSORPTION OF 02 ON SILICA-GEL ALUMINA-GEL AND
BRINE 4300S
RYLULB60CC
CHEMICAL EQUILIBRIA IN INORGANIC SYSTEMS
PHYSIOCHEMICAL FORCES IN A CRYSTAL LATTICE
EQUILIBRIUM OF
KAPUAF36CEU
VANADIUM MODIFIED CRYSTALLINE ALUMlNQSILICATES AND THEIR
PROPERTIES • LEVISA65VMC
A NEW APPROACH TO THE STUDY OF ACTIVE CENTER OF CRYSTALLINE
CATALYSTS PQLTGM66ANA
COMPARATIVE CATALYTIC ACTIVITY OF CENTERS ON THE
CRYSTALS AND OF AN INERT CARRIER
SELECTIVITY OF SUCCESSIVE REACTIONS IN CYLINDRICAL CATALYSTS
WAKAN 66SOS
REMOVING IRON FROM REACTIVATED OIL TREATMENT CATALYSTS
CONTAINING PLATINUM LFOPJG65RIF
SURFACE OF
5TRE.ZV64CCA
10/27/69
DEACTIVATED
REACTIVATION
11ECAY
DECAYING
DECOMPOSITION
DEPENDENCE
DESIGN
PAGE 27
REGENERATION AND REACTIVATION OF DEACTIVATED PLATINUM
CATALYST ON A CARRIER SHEL
62RAR
SOME TOPICS IN OPTIMIZATION Of REACTORS WITH CATALYST
DEACTIVATION CHOUA 67STO
THE OEACTIVATION OF CATALYSTS AND SOME RELATED OPTIMIZATION
PROBLEMS SZE"S 670CS
SIMPLE CONTROL POLICIES FOR REACTORS WITH CATALYST DECAY
CHOUA 67SCP
A THEORETICAL TREATMENT OF CATALYST DECAY HOJCBW68TTC
CONTROL OF A COLD SHOT ADIABATIC
DECAYING CATALYST
BED REACTOR WITH A
LEF. KY6JCOA
DECOMPOSITION PRESSURES OF NITRATES AND SULFATES
MEASUREMENTS OF SOOIUM-VANAOATFS NEUMB 350PO
DEPENDENCE OF THE CATALYTIC ACTIVITY OF THF
V2P5 ON ITS MODE OF COMBINATION WITH SILICA
ADAOIE2<>nOT
LACK OF DEPENDENCE OF CONVERSION ON FLOW RATE IN CATALYTIC
STUDIES CHAMRP66LOD
ALLOWANCE FOR THE TEMPERATURE DEPENDENCE OF SPECIFIC H>=AT
OF INDIVIDUAL GASES AND GAS MIXTURES IN THEPMODYNAMIC
CALCULATION FOR GAS FLOW MACHINE FISCS 6SATD
DEPENDENCE OF THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE ON
THE PARTICLE SIZE OF THE CATALYST IN AGITATF.D AND
FIXED-BEDS SCHYF 61DOT
DEPENDENCE OF CATALYTIC ACTIVITY OF METAL ON THEIR POSITION
IN PERIODIC TABLE SCKDAMf.600C
DESIGN OF MULTISTAGE CONVERTER FOR 502 OXIDATION
ABE K SODOM
DESIGN OF CONTACT PROCESS EQUIPMENT WITH AN AniABATIC
CATALYST LAYER FOR THE OXIDATION OF SULFUR-DIOXIDE DESIGN
OF EQUIPMENT WITH THE INTRODUCTION OF COLO REACTION
MIXTURES AND WITH INTERMEDIATE HEAT EXCHANGERS
THE DESIGN OF A UNIT FOR THE SYNTHESIS OF
SULFUR-TRirxIOE
BRUSH 66004
r.ALOPH5*CPC
CONTACT PROCESS CONVERTER DESIGN
DESIGN OF FIXED-BED TUBULAR CATALYTIC REACTORS
CARRS 6200F
DESIGN OF UNIFORM-FLOW TOWERS WITH CENTRIFUGAL ATOMIZERS
GANZSN65DUF
CONTACT REACTION RATE OF S02 OXIDATION APPLICATION OF THE
RATE EXPRESSION TO NEW OBSERVATIONS AND ILLUSTRATION FOR
THE CONVERTER DESIGN HARAH S9CRR
PRINCIPLES OF REACTOR DESIGN GAS-SfUin INTTRFACE
DESIGN DF FIXFD-BFD CATALYTIC KFACIflRS
DCS ION np A CATALYTIC REACTOR
I"-'VIM**1OHF
KONI^ S?DOA
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10/27/69
DESIGN
DFSIGNING
OESULFURI7ATION
DESULFURIZING
DETECTION
DETECTOR
DETERIORATION
DEW-POINT
DIFFUSION
PACE 28
DESIGN OF FIXED-BED TYPE CONVERTER FOR S02 OXIDATION
KUBOH 60DOF
DESIGN CALCULATIONS FOR PROCESSES IN FIXED-BEDS AND
FLUIOIZEO-BEDS OF CATALYST KUZ1VA65DCF
DIFFUSION IN CATALYSIS CRITERIA FOR THE. DESIGN OF AN
EXPERIMENTAL REACTOR PARAA 64DCC
DESIGN OF AN INSTALLATION FOR RETAINING OF S02 CONTAINING
RESIDUAL GASES IN A PLANT OF COMPLEX FERTILIZERS UNDER
ECONOMICALLY ADVANTAGEOUS CONDITIONS POPON 67DIR
DESIGNING OF CONTACT APPARATUS FOR THE OXIDATION OF
DIOXIDE BESKVS65DOC
DETERMINING THE RETARDATION DEGREE OF THE THERMAL
DESULFURIZATION OF HIGH ASH PETROLEUM COKES
ABYZYM670TR
UTILIZATION OF HIGH-VOLTAGE ELECTRIC FIELDS FOR THE
DESULFURIZATION OF FLUE-GAS ACS M 66UOH
THE PRESENT POSITION OF FLUE-GAS OESULFURlZATION
THE CURRENT TECHNICAL SITUATION OF DESULFURIZATION OF
PETROLEUM TAKAIT67TCT
DESULFURIZING FINE
OESULFURIZING OF F
BERG 630FG
KLIMR 65DFG
DETECTION OF PHOTOCHEMICAL OXIDATION OF SULFUR-DIOXIDE
DUNHSB6PDOP
THE DETECTION OF PREMATURF GRADUAL CHANGES OF THE SURFACE
LAYER OF SOLID BODIES AS ILLUSTRATED BY V205
DETECTOR FOR GASEOUS COMPONENTS WITH SEMICONDUCTT VE THIN
FILMS SEIYT 66DSC
DETERIORATION IN SERVICE OF VANADIUM CATALYSTS USED FOR
OXIDATION OF SULFUR-DIOXIDE S1ROGD4BDIS
MEASUREMENT OF THE DEW-POINT OF FLUE-GASES AND ITS EFFECT
ON THE START OF CORROSION • ROEGH 64MDP
DIFFUSION AND HETEROGENEOUS REACTION
DIFFERENT CATALYST GEOMETRIES
DIFFUSION PROCESS IN GAS HETEROGENEOUS GAS CATALYSTS
EFFECTA§FLOCM65DHR
CATALYTIC OXIDATION
RAPID CATALYTIC
DIFFUSION TUBES
IN TO SULFUR-TRIOXIOE
PROCESSES II. GENERA
EFFECT OF DILUTION
ALDEH 62DPI
'E AND THE THEORY OF
AL RULE FOR GAS
WITH INERT GASEf
ANDRL -
POPOUS-BED DIFFUSION USING THE FREQUENCY RESPONSE METHOD
KINETICS OF REVERSIBLE CATALYTIC REACTIONS IN THE INTERNAL
DIFFUSION RANGE BOREGK52KOR
10/27/69
DIFFUSION
DIFFUSIVE
DISCHARGE
DRY
DRYING
PAGE 29
HEAT TRANSFER ANALOGY FOR DIFFUSION AND FIRST ORDER CHEMICAL
REACTION IN A CATALYST PORE COUGRW67HTA
DIFFUSION AND REACTION RATE HARAY
PORE STRUCTURE AND GASEOUS DIFFUSION IN SOLID CATALYSTS
JOHNMF65PSA
PORE STRUCTURE AND GASEOUS DIFFUSION IN SOLID CATALYSTS
JOf ~
DIFFUSION
JOHNMF65PSG
KRASJH55EFW
EFFECTIVENESS FACTORS WITH SURFACt
EFFECTIVENESS FACTORS WITH SURFACE DIFFUSION KRASJH65EFS
THE INFLUENCE OF EXTERNAL DIFFUSION INHIBITION ON THE
PROCESS IN A POROUS CATALYST LEVIVG66TIO
FLUIDIZED-BED DIFFUSION MALLWC67FBO
DIFFUSION IN CATALYSIS CRITERIA FOR THE DESIGN OF AN
EXPERIMENTAL REACTOR PARAA 64DCC
EFFECT OF INTERNAL DIFFUSION ON CATALYTIC REACTIONS I
IRREVERSIBLE REACTION WITHOUT A CHANGE IN THE NUMBER OF
MOLES . SCHNP 65EOI
EFFECT OF INTERNAL DIFFUSION ON CATALYTIC REACTIONS
EFFECT OF PARTICLE SHAPE ON REACTION WITH LANGMUIR
HINSHELWOOD TYPE OF KINETICS SCHNP 66EID
DIFFUSION PHENOMENA IN HETEROGENEOUS CATALYSIS
SHEPTK65DPI
SELECTIVITY FOR SUCCESSIVE FIRST ORDER REACTION AND CATALYST
PORE STRUCTURE DURING HIGH DIFFUSIVE RESISTANCE PROCESSES
TARTR 67SSF
ELECTRIC DISCHARGE APPARATUS FOR THE SYNTHESIS OF
NITRIC-OXIDE FROM ATMOSPHERIC NITROGEN COTTWJ49EDA
CHEMICAL REACTIONS BY ELECTRICAL DISCHARGE HOLMWC65CRB
EQUIPMENT TO CHARGE AND DISCHARGE CATALYST PACKING OF
THI
IYNTHESIS MULTILAYER REACTORS KIIBEJ 67ECD
' OXIDATION OF SULFUR-DIOXIDE IN A ELECTRODELESS DISCHARGE
MAHASD32TOO
OXIDATION OF SULFUR-DIOXIDE IN A HIGH-FREQUENCY DISCHARGE
POSSIBILITY OF THE INFLUENCE OF LONG WAVES OF A
HIGH-FREQUENCY DISCHARGE ON GASEOUS CHEMICAL REACTIONS
ZALON 35POT
REDUCING DISCHARGE INTO THE ATMOSPHERE OF SULFUR IC-AC10 MIST
MINIMIZING SULFURIC-ACID VAPOR DISCHARGE INTO THF
ATMOSPHERE. ZILPDE68ROI
EVALUATION OF PRY PROCESSES FOR REMOVING S02 FROM POWER
PLANT FLUE GASES BIENO J.SEOP
ABSORBING SULFUR-DIOXIDE ON DRY ION-EXCHANGE ROSINS
COLER 60ASD
DRY SEPARATION OF SULFURrDIOXIDE FROM WASTE GASES
JUENH 6ISDSS
LIMESTONE MILL DRYING PLANTS FOR THE REMOVAL OF
FROM WASTE AND FLUfc-GASES ...
AN AUTOMATIC CONTROL SYSTEM FOR THF DRYING AND ABSORPTION
S02
HPHMH 67LMD
CYCLE IN SULFURIC-ACID PRODUCTION
IGREV 67ACS
C3
-------
•TJST
DYNAMICS
ECONOMIC
PAGE 30
AIKALINF EARTH MFTAL COMBINATION WITH SD2 OF FLUE-GAS
'IN A FLUE OUST CLOUD
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10/27/69
ELECTROCHEMICAL
PAGF
32
KLYAGL62TPO
ELECTRODE
ELECTROOELESS
FLECTRODES
ELECTROLYSIS
ELECTROLYTIC
THE POSSIBILITY OF ELECTROCHEMICAL OXIDATION OF
SULFUR-DIOXIDE BY ELECTROLYTIC OXYGEN .-_
MECHANISM OF OXIDATION HYDROGENATION AND ELECTROCHEMICAL
COMBUSTION ON SOLID CATALYSTS LOW TEMPERATURE
OXIDATION ON PLATINUM OVCHEN61MOO
ELECTROCHEMICAL PROCESS OF PRODUCING ELECTRICAL ENERGY BY
USING SULFUR-DIOXIDE FUEL AND HALOGEN OXIDANT
RIGHRA67EPO
DETERMINATION OF THE NUMBER OF ACTIVE CENTERS ON THE CARBON
SURFACE BY THE ELECTROCHEMICAL METHOD IN OXYGEN
CHEMISORPTION SIEOJ 65DNA
ELECTROCHEMICAL METHOD OF PRODUCTION OF SULFURIC-ACID
SUSHAM63E MO
RPLE OF CATALYTIC FACTORS IN THE ELECTROCHEMICAL REACTIONS
VESEVI55ROC
APPLICATION OF THE POWDER ELECTRODE TO THE EXAMINATION OF
THE COURSE OF CHEMICAL REACTION ON A CATALYST
TOMAW 60AOT
THE OXIDATION OF SULFUR-DIOXIDE IN A
PLASTIC-BONDED ELECTRODES
INFLUENCE OF THE ULTRASONIC FIELL
OF MN02 PREPARED BY ELECTROLYSIS
ELECTROOELESS DISCHARGE
MAHASD32TOO
ADLHOJ67PBE
ON THE CATALYTIC ACTIVITY
KOWAE 651UF
THE MECHANISM OF THE ELECTROLYTIC OXIDATION OF
SULFUR-DIOXIDE
ZINC RECOVERY AT
BOGOGAS8TMO
ELECTRON
ELECTROCHEMICAL OXIDATION OF
SULFUR-DIOXIDE BY ELECTROLYTIC OXYGEN
ELECTROLYTIC PRODUCTION OF SULFURIC-ACID
THE STRUCTURE OF SUPPORTED PLATINUM CATALYSTS
_BY_ELECTRON MICROSCOPY
SEMICONDUCTANCE AND
.._ CANADIAN ELECTROLYTIC ZINC'S NEW
VALLEYFIELD PLANT JEPHAC66ZRC
EFFECT OF LOW-COST ELECTROLYTIC HYDROGEN ON THE GENERATION
OF BASIC CHEMICALS JUDAW 67EOL
THE PgSSIB!LITV_OF ELECTRgCHEMICAL_OXiDATION OF
VASISVSOEPO
EXAMINATION
MOSSRL67SSP
TE
.. riNG MIXED CATALYSTS OF
...^ . CALITE-fYPE III. RELATION ._..-_
ACTIVITY STOICHIOMETRIC COMPOSITION AND RATE OF ELf.CTRON
LINKAGE FOR P-CONDUCTING MIXED CATALYSTS OF THE HOPCALIJE
TYPE RIENG A4SAC
CHANGES IN THE CONDUCTIVITY AND WORK-FUNCTION OF JHEr_,
ELECTRON UPON ABSORPTION OF 0 AND S02 AND V205 LAYERS
5URNLN65CIT
ELECTRON-MICROSCOPIC ^^ Qf ^ p ,. STRU(-TURE ^ ^
VANADIUM CATALYST FOR SO? OXIDATION KARADR65EMS
SPftKKc
THE HOPCAL
TALYSIS RELATION BETWEEN
IQICH1
HIOMETRIC COMPOSITION AND STA
-CONDUCTING MIXED CATALYSTS OF
ELATION BETWEEN CATALYTIC
10/27/69
ELECTRONIC
PAGE
33
ELECTRONS
ELECTRONIC CONFIGURATION AND HETEROGENEOUS CATALYSIS
COMPARATIVE RESULTS FOR THERMAL AND ELECTRONIC ACT?VAT 101^0*
MIXTURES OF SULFUR-DIOXIDE AND OXYGEN MOYEAJ65CRF
THE.ELECTRONIC MECHANISM OF THE CATALYTIC FORMATION OF S03
ELECTRONIC MECHANISM OF THE CATALYTIC 503 FORMATIONHONMCRf03
ELECTRONIC FACTOR IN CATALYSIS AND SELECTION OF CATALYSTS6"0
ELECTRONIC THEORY OF CATALYSIS WOLKT^feETC
ELECTROSTATIC PRECIPITATOR _ ., _
ELECTROSTATIC DEPOSITION OF SULFURIC-ACID MISTS FROM THE
META 641 PR
ORNEN 6&EP
HASTE GASES OF SULFURIC-AC ID MANUFACTURE
STOP* 65EDS
ROLES OF ELECTRONS HOLES AND LATTICE DEFFECTS IN
HETEROGENEOUS CATALYSTS HAUFK 65REH
OXIDATION OF SULFUR-DIOXIDE CAUSED BY IMPACTS OF SLOW
ELECTROOXIDATION ELECTRONS STUPEV4900S
MECHANISM OF ELECTROOXIDATION OF SOME COMPOUNDS ON PLATINUM
ELECTROPRECIPITATION SHLYAI56MOE
ELECTROPRECIPITATION METHOD AND EQUIPMENT LODG 6C.EME
CONDITIONING OF FLUE-GASES IN BOILER PLANTS FOR IMPROVEMENT
OF DEGREE OF SEPARATION OF ELECTROSTATIC FILTERS
CONDITIONING OF STACK GASES FOR ELECTROSTATIC PRECIPI TATORS_
INCREASED PRECIPITATION RATE OF ELECTROSTATIC
ENERGY
ENGINEERING
ENTROPY
EQUATION
EQUATIONS
EFFECTS OF CARRIERS AND DILUENT ON THE ENERGY OF ACTIVATION
AND THE VALUE OF THE DISPERSION COEFFICIENT
RELATION BETWEEN REACTION ORDER AND ENERGY OF ACTIVA?!oN6ECD
OF DIRECT AND INVERSE REACTIONS BOREGK45RBR
ELECTROCHEMICAL PROCESS OF PRODUCING ELECTRICAL ENERGY BY
USING SULFUR-DIOXIDE FUEL AND HALOGEN OXIDANT
RIGHRA67EPO
ENGINEERING ASPECTS OF CATALYTIC REACTIONS
CHEMICAL ENGINEERING ASPECTS FOR
- -_ ._ CARBJJ67EAC
«*« -D.FV~-~:;~« SULFUR-DIOXIDE REMOVAL
FROM WASTE-GASES JUENH CEA
CHEMICAL ENGINEERING ASPECTS FOR SULFUR-DIOXIDE REMOVAL FROM
WASTE-GASES JUENH 65CEA
ENTROPY OF THE ACTIVE COMPLEX IN THE OXIDATION OF
SULFUROUS-ANHYDRIOE OVER PT CATALYST
A MODIFIED REDLICH-KWONG EQUATION II F STATF
GOLOGI61EOT
BARNHF66MRK
KINETIC STUDIES ON THE OXIDATION OF SULFUR-DI OX I HE ON
VANADIUM CATALYSTS III. A COMPARISON OF THE
.
OBTAINED WITH SOME INDUSTRIAL
RATE EQUATIONS
VANADIUM CATALYSTS
CHANMfS9KSn
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10/77/69
EOUATIONS
EQUILIBRIA
EQUILIBRIUM
EQUILIBRIUMS
EXCHANGE
EXCHANGER
EXCHANGES
EXHAUST-GASES
EXOTHERMIC
PAGE
NUMERICAL SOLUTION OF TWO-POINT ROUNORY VALUE PROBLEM VALUE
PROBLEMS IN SIMULTANEOUS SECOND-ORDER NONLINEAR ORDINARY
DIFFERENTIAL EQUATIONS LIU SL67NSO
ALGEBRAIC MANIPULATIONS OF THE RATE EQUATIONS OF CERTAIN
CATALYTIC REACTIONS WITH A DIGITAL COMPUTER
QUALITATIVE ANALYSIS OF EQUATIONS DESCRIBING EXOTHERMIC6
PROCESSES CATALYTIC PROCESS IN A POROUS PLATE
ZELETI660AD
CHEMICAL EQUILIBRIA IN INORGANIC SYSTEMS EQUILIBRIUM OF
PHYSIOCHEMICAL FORCES IN A CRYSTAL LATTICE KAPUAF36CEU
EQUILIBRIUM PRESSURE OF SULFUR-TRIOXIDE VAPORS OVER OLEUM
AKSEYV64EPS
EQUILIBRIUM POSITION AND KINETICS OF OXIDATION OF
SULFUR-DIOXIDE AND SYNTHESIS OF AMMONIA ANDRL 61EPA
THE KINETICS OF OXIDATION OF SULFUR-DIOXIDE ON A PLATINUM
CATALYST UNDER EQUILIBRIUM CONDITIONS ROITVA60TKD
INVESTIGATION OF THE KINETICS OF THE PROCESS
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10/27/69
FACTORS
FERRIC-HYDROXIDE
FERRIC-OXIDE
FERRUNuINOUS
PACE
36
FERTILIZER
FERTILIZERS
FILTER
FILTERING
FILTERS
FIXED-BED
FLOW
PF CATALYTIC FACTORS IN THE ELECTROCHEMICAL REACTIONS
VESEVI55ROC
CATALYTIC PROPERTIES OF FERRIC-HYDROXIDE IN THE OXIDATION OF
SULFUR-DIOXIDE BY ATMOSPHERIC OXYGEN -
KINETICS OF CONTACT OXIDATION OF SULFUR-DIOXIDE
PRESENCE OF FERRIC-OXIDE
TALIM 37CPO
IN THE
BOREGK44KOC
SULFURIC-ACID AND FERTILIZERS VAHETK67S
SIMULTANEOUS RECOVERY OF SULFUR-DIOXIDE AND THE PRODUCTION
OF NITROGEN FERTILIZERS VASINA60S
PROCESS FOR EXTRACTION OF VALUABLE PRODUCTS FROM SCHISTS
AND OTHER BITUMINOUS FERRUNGINOUS AND SULFUROUS SEDIMENTS
AND COMPOUNDS MANUFACTURED THEREFROM LUPAK 66PEV
COMPOSITE FERTILIZER FROM PHOSPHATE NITRIC-ACID AMMONIA AND
SUL'FUR-DIOXIDE NA8IMN67CFF
DISPOSAL OF WASTES IN A PHOSPHATIC FERTILIZER PLANT
PANDSR6SOWP
K67SAA
T I ON
INA60SRS
FILTER MASS FOR THE REMOVAL OF SULFUR-DIOXIDE FROM WASTE
GASES EHREW 66FMR
CONSTRUCTION MATERIALS 'FOR FILTERING APPARATUS IN
NICKEL COBALT PRODUCTION SHVAGL63CMF
CONDITIONING OF FLUE-GASES IN BOILER PLANTS FOR IMPROVEMENT
OF DEGREE OF SEPARATION f)F ELECTROSTATIC FILTERS
OARBK 66CFG
GLASS-WOOL FILTERS FOR TRAPPING SULFURIC-OXIDE MIST
VASHEV65GWF
DESIGN OF FIXED-BED TUBULAR CATALYTIC REACTORS
FIXED-BED CATALYTIC REACTORS I. MAIN PROBLEMS
CARRS 62DOF
GIGNJ 67FBM
DESIGN OF FIXED-BED CATALYTIC REACTORS IRVIHB5100F
FIXED-BED CATALYTIC REACTORS II. ONE DIMENSION STATIC MODELS
WITHOUT HEAD LOSSES KAZIC 67FBO
OPTIMUM CONDITIONS FOR GAS-SOLID CATALYTIC REACTION PROCESS
IN A FIXED-BED KUROH 590CF
DESIGN OF FIXED-BED TYPE CONVERTER FOR 502 OXIDATION
KUBOH 60DOF
IMPROVEMENTS IN FIXED-BED CATALYST OPFRATIflNS
MAC.KJ OTiFB
LACK OF DEPENDENCE OF CONVERSION ON FLOW RATE IN CATALYTIC
STUDIES CHAMRP66LOO
ALLOWANCE FOR THE TEMPERATURE DEPENDENCE OF SPECIFIC HEAT
OF INDIVIDUAL GASES AND GAS "IXTURES IN THEPMODYNAMIC
CALCULATION FOR GAS FLOW MACHINE FISCS 6SATP
71
10/27/69
FLOW
FLOW-SHEETS
FLUE-GAS
FLUE-GASES
PAGE 37
FLOW OF SULFUR-DIOXIDE OVER THE SURFACE OF SPHERON-6(2700)
GRAPHITIZED CARBON BLACK POPECG67FSD
CONTROL FLOW-SHEETS IN THE OPERATION OF SULFURIC-ACID
CONTACT INFORMATION PETRNM66CFS
UTILIZATION OF HIGH-VOLTAGE ELECTRIC FIELDS FOR THE
DESULFURIZATION OF FLUE-GAS ACS M 66UOH
PROBLEMS OF CORROSIONS AND DEPOSITS ON THE FLUE-GAS SIDE
OF HEATING SYSTEMS BERGP 57PCD
THE PRESENT POSITION OF FLUE-GAS DESULFURIZATION
BREN 65PPF
RECOVERY OF SULFUR FROM FLUE-GAS BY THE USE OF AMMONIA
CRAXSR5ZRSF
PRODUCTION OF SULFURIC-ACI0 FROM FLUE-GAS FROM OIL TREATMENT
DEGTIP66POS
FLUE-GAS PROCESS
FLUE-GAS CORROSION REDUCTION
WET SCRUBBING OF BOILER FLUE-GAS
TREATMENT OF FLUE-GAS
SULFUR-OXIDES IN FLUE-GAS AND IN THE ATMOSPHERE
KEEPING THE AIR PURE
OUNORH67FGP
HOUS 67FGC
KOPIR 6BWSB
KUESW 65TOF
A PROBLEM OF
SPENG 65SOI
CONDITIONING OF FLUE-GASES IN
OF DEGREE OF SEPARATION OF
BOILER PLANTS FOR IMPROVEMENT
ELECTROSTATIC FILTERS
SCRUBBING OF SULFUR-DIOXIDE FROM FLUE-GASES
REMOVAL OF SULFUR COMPOUNDS FROM FLUE-GASES
CATALYTIC OXIDATION OF SULFUR-DIOXIDE PRESENT
BY IONIZED SOLUTIONS OF HEAVY METALS
LIMESTONE MILL DRYING PLANTS FOR THE REMOVAL OF
FROM WASTE AND FLUE-GASES
REMOVING SULFUR-DIOXIDE FROM FLUE-GASES
THE REMOVAL OF SULFUR-DIOXIDE FROM FLUE-GASES
DARBK 66CFG
GEMER 65SSD
GRILW 66RSC
IN FLUE-GASES
GRODNK33COP
S02
HOHMH 67LMD
KATES 66RSO
OESULFURIZING
SULFUR-OXIDES
OF FLUE-GASES
REMOVAL FROM FLUE-GASES
SULFUR-DIOXIDE REMOVAL OF FLUE-GASES
DETERMINATION OF S02 AND ACID DEW '
ANTIPOLLUTION PROCESS USES ABSORBENT TO REMOVE
'-GASES
SULFUR-DIOXIDE
KETTH 65TRO
KLIMR 65DFG
KRIZM 655OR
KRUEM 67SDR
OINT IN FLUE-GASES
LISLES6500S
• HI IPULLUI IUN PKULtii U5C5 ABiUKC
SULFUR-DIOXIDE FROM FLUE-GASES
MULTISTAGE PURIFICATION OF FLUE-G
PURIFICATION OF FLUE-GASES FROM 5
REMOVING
THE
RE
FLUE
WING SULFUR-DIOXIDE FR(
SIMULTANEOUS ABSORPTIOI
DUCED SULFUR COMPOUNDS
UE-GASES
MDNFG 63PFG
MTENP65RSD
ONE OR MOR
ESPECIALLY
FROM FLUE-GASES
~~N OF SULFUR-OXIDES AND
INDUSTRIAL GASES
REINLU65SAS
AND ITS EFFECT
_. — . __- __ — ____-- ROEGH onHDP
OF OUST FROM FLUE-GASES ROLLL 67RDF
OF CARBON-MONOXIDE AND SULFUR-ACIDS FROM FLUE-GASES
TILHR 66RCM
MEASUREMENT OF THE DEW-POINT OF FLUE-GASES
ON THE START -~
REMOVAL
REMOVAL
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10/27/69
I-LUE-GASES
FLUIDIZABLE
FLUIDIZED
REMOVAL OF SULFUR-DIOXIDE FROM FLUE-GASES
GAS PHASE OXIDATION PROCESS
PAGE 38
THE BCR CATALYTIC
ZAWAEA65ROS
CONTACT OF FLUIDIZABLE SOLIDS WITH GASEOUS FLUIDS
ADAMCF67CFS
MEANS AND METHOD FOR AUTOMATIC ADDITION OF FINELY DIVIDED
PARTICLES TO A FLUIDIZED CONTACTING SYSTEM ADAHFH66MMA
CALCULATIONS FOR FLUIOIZED BED CATALYTIC EQUIPMENT
ANOK 65CFF
STORING AND STRIPPING CATALYST IN A FLUIDIZED SYSTEM
BELODH65SSC
THE USE OF FLUIDIZED CATALYST FOR THE OXIDATION OF
BERAY 57TUO
OXIDIZING SULFUR-DIOXIDE BY USING FLUIDIZED IRONIIIII OXIDE
BLICT 610SO
PRODUCTION OF CATALYSTS IN A FLUIDIZED LAYER FOR OXIDATION
. SULFUR-DIOXIDE
GRADLI62POC
UIDIZFD BED
GRADLI63COO
SULFUR-OIOXIOL
MUKHIP55TUO
SULFUR-DIOXIDE IN
CATALYTIC OXIDATION OF SULFUR-DIOXIDE GAS IN A FLUIDIZFD BED
GRADLI63COG
FLUIDIZED BED PROCESSES JAVOJ 66FBP
OXIDATION OF S02 IN A FLUIDIZED CATALYST BED KERNVS6600S
KINETICS OF SORPTION AND OF THE CHEMICAL REACTION ON A
UNIFORM-SURFACE CATALYST IN A FLUIDIZED BED INVOLVING
COMPLETE INTERMIXING OF PARTICLES AND OF THE GAS
LAVOKP64KOS
HEAT REMOVAL FROM FLUIDIZED SOLID REACTOR BEDS
LEWIK A9HRF
FLUIDIZED HETEROGENEOUS CATALYSIS BY THE METHOD OF CURRENTS
MERTE H TFHC
THE USE OF A FLUIOIZEO CATALYST FOR SULFUR-DIOXIDE
OXIDATION
NEW CONTACT APPARATUS FOR THE OXIDATION OF
A FLUIOIZED CATALYST BED MUKHIP59NCA
~ ' UTACT EQUIPMENT WITH A FLUIDIZED CATALYST BED
ING OF SULFURIC-ACID MUKHIP63TUO
._ FRATED SULFUR-DIOXIDE IN A FLUIDIZED
LAYER OF WEAR RESISTANT VANADIUM CATALYST MUKHIP6500C
PERFORMANCE OF AN INDUSTRIAL APPARATUS FOR THE OXIDATION OF
S02 IN A FLUIDIZED CATALYST BED RUMAES66POA
OXIDATION OF SULFUR-DIOXIDE IN A FLUIDIZED BED WITH VANADIUM
CATALYST SZOLP 5500S
KINETIC ANOMALY OF CATALYTIC CONTACT REACTIONS IN A
FLUIDIZED LAYER OF SHALL DIMENSIONS SZOLP 62KAO
OVERALL RATE OF CATALYTIC REACTIONS AS INFLUENCED BY THE
___ TODEOM&60RO
CATALYST B~
TRABOG59K
OX I OAT ION OF SULFUR-DIOXIDE ON FLUIDIZED VANADIUM CATALYST
VARLML5400S
CONTINUOUS REMOVAL OF SULFUR-DIOXIDE FROM GAS MIXTURES
BY A FLUIDIZED LAYER OF SOLID GRANULAR ABSORBENT
THE USE OF CON1
IN ~
... THE MANUFACTURE- _
OXIDATION OF CONCENTRATED
INHOMOGENEITY OF THE FLUIDIZED BED
KINETICS OF THE OXIDATION OF SO2 IN A
FLUIDIZED CATALYST BED
TRABDG59KOT
VANADIUM CATALYSTS
73
lO/Z7/<>9
f-LUiDizEO-BEo
FLUIDIZED-BEflS
FLUME
FLUX
FOULED
FREE-ENERGY
PAGE
39
THE HYDRODYNAMIC MODEL OF a FL UI Dl ZED-BED ABAEGN6«TH»
THE DYNAMICS AND CONTROL OF AN EXOTHERMIC REACTION IN A
FLUID1 ZED-BED REACTOR BARNLA65TDA
POISONING OF VANADIUM CATALYST IN A FLUI 01 ZED-BED WITH
ARSENIC-TRIOXIDE IVANRS67POV
CALCULATION OF THE FLUIDIZED-BED CATALYTIC PROCESS
K P PKiut A ^f" CQ
OXIDATION OF SULFUR-DIOXIDE IN A FLUID I ZED-BED CATALYST
KUZMIN&inOS
APPARATUS FOR CONTACT OXIDATION OF SULFUR-DIOXIDE WITH A
FLUIDIZED-BED OF CATALYST LABUGV59AFC
OXIDATION OF S02 IN AN APPARATUS WITH A FLUID! ZED-BED OF FE-
OXIDE CATALYST DURING H2SO* PRODUCTION BY THE -------
PROCESS
FLUIDIZED-BED DIFFUSION
IMPROVEMENTS IN A FLUI DI ZED-BEO PROCESS
EFFECT OF WATER VAPOR AND IRON COMPOUNDS ON THE
OF VANADIUM CATALYSTS IN A FLUIDI ZED-BED .._ ..... _..
POISONING OF VANADIUM CATALYSTS USED IN THE OXIDATION OF
SULFUR-DIOXIDE IN A FLUIDIZEn-BED "IUKHIP65POV
STRUCTURE OF WEAR RESISTANT VANADIUM CATALYSTS FPR
SULFUR-DIOXIDE OXIDATION IN A FLUIDIZEn-BED
MUKHI P6TSHR
VANADIUM ON ALUMINA CATALYST FOR FLUID I ZED-BED OXIDATIONS
Nl TT 65VOA
POROUS SUPPORT FOR FLUI 01 ZED-BED CATALYSTS SELIHJ67PSF
ITH FLUIDIZED-BED OF POWDERED CATA
CONTACT
LASTYV6ISOOS
MALLWC67FBD
HCILAE66IFB
ACTIVITY
MUKHIP&3EOW
TALYST
LABORATORY APPARATUS WITH FLUIDIZED-BED OF POWDERE
EFFECT OF PARTICLE SIZE OF A VANADIUM CATALYST
ACTIVITY IN THE FLUIDI ZED-BED OXIDATION OF SULFUR-DIOXIDE
TPABOG59EOP
GAS MIXING AND MOVEMENT OF SOLID PARTICLES IN A
FLUIDIZEO-BED TRABOG62GMA
«
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FREE-ENERGY
FREE-RADICALS
FUMES
FURNACE
FURNACES
CAS
PAGE
LINEAR FREE-ENERGY-RELATIONSHIPS IN HETEROGENEOUS CATALYSIS
IV. REGIONAL ANALYSIS FOR SOLID ACIO CATALYSIS
YONEY 67LFE
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE~CONTRIBUTION OF CARBON FREE-RADICALS IN THE
SO? TO SOB OXIDATION PROCESS SIEDJ 65MCO
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THE CONCENTRATION OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND S02 OXIDATION
PROCESSES SIEOJ 66HCO
A CATALYST FOR OXIDATION OF AUTOMOBILE AND INDUSTRIAL FUMES
KEITC065ACF
REMOVAL OF NITROGEN-OXIDE CONTAINING SULFURIC-ACID FUMES
LANMC 66RNO
RECOVERY PROCESS FOR LOW CONCENTRATIONS OF GASEOUS SULFUR
COMPOUNDS CONTAINED IN RESIDUAL GASES AND FUMES
PIERRJ66RPL
COMPLETION OF THE OXIDATION OF S02 CATALYST FURNACE OF A NEW
TYPE IN A H2S04 PLANT ALMAG 63COT
MODERN TECHNIQUES OF STUDY OF CORROSION AND ATMOSPHERIC
POLLUTION APPLIED TO BOILERS AND FURNACES ETOCP.66MTS
TYPES OF CORROSION AND BEHAVIOR OF METALS
BOILER FURNACES
AND
ADDITIVES IN
WICKK 65TCB
DIFFUSION PROCESS IN GAS HETEROGENEOUS GAS CATALYSTS
ALDEH 62DPI
PURIFYING A GAS MIXTURE FROM SULFUR-DIOXIDE AMELAG67PGM
CATALYTIC OXIDATION TO SULFUR-TRIRXIOE AND THE THEORY OF
RAPID CATALYTIC PROCESSES II. GENERAL RULE FOR GAS
DIFFUSION TUBES EFFECT OF DILUTION WITH INERT GASES
ANORL 53COT
STRUCTURAL CHARACTER IZAT ION OF CATALYSTS INTERPRETATION
OF DATA ON GAS ABSORPTION ASENJ 67SCP
CARRYING OUT EXOTHERMIC CATALYTIC GAS REACTIONS SUCH AS
OXIDATION OF SULFUR-01 OX IDE BAVEJ 35COE
ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE AQUEOUS
SOLUTION FROM A GAS MIXTURE BLASH 66ASO
INITIATING A HOMOGENEOUS REACTION IN A GAS BY SOLID CATALYST
BOGOML46IAH
REMOVING SULFUR-TRinXIDE FROM GAS MIXTURES BURKDB68RST
UTILIZATION OF AMMONIUM-SULFITE SOLUTIONS FROM THE FINAL GAS
SCRUBBING SOLUTION OF THE CONTACT SULFURIC-ACID
INSTALLATIONS CHEM 64UAS
EFFECT OF A POROUS SILICA-GEL CATALYST CARRIER ON THE
VELOCITY OF OXIDATION OF SULFUR-DIOXIDE GAS
CHUFGI34EOA
EXOTHERMIC GAS REACTION SUCH AS OXIDIZING SULFUR-DIOXIDF TO
TRIOXIOE ._ ftCLARCB27EGP
CLUZJ 6SFAR
FIXATION AND RECOVERY AS AMMONIUM-SULFATf OF WA
DIOXIDE IN INDUSTRIAL EFFLUENT GAS
75
10/27/69
GAS
PAGE
IMPROVEMENT OF THE MASS TRANSFER FPOM A GAS TO A POROUS
CATALYST OR ADSORBENT BY PRESSURE OSCILLATIONS
APPARATUS FOR AFFECTING GAS REACTIONS BY MEANS OF ELECTRICAL
DISCHARGES FARB 30AFA
CONTACT MASSES FOR HETEROGENEOUS GAS CATALYSIS
FARB 56CMF
CATALYTIC GAS REACTIONS FARBIG35CGR
INSTALLATIONS FOR INDUSTRIAL GAS CLEANING PROCESS
OPTIMIZATION FOR OPERATING MULTIPLE INSTALLATIONS IN ANY
REGIME FERRG 661FI
ALLOWANCE FOR THE TEMPERATURE DEPENDENCE OF SPECIFIC HEAT
OF INDIVIDUAL GASES AND GAS MIXTURES IN THERMODYNAMIC
CALCULATION FOR GAS FLOW MACHINE FISCS 65ATD
CATALYTIC OXIDATION OF SULFUR-DIOXIDE GAS IN A FLUIOIZED BED
GRADLI63COQ
ECONOMIC ELIMINATION OF AIR POLLUTION THROUGH RECOVERY
PRODUCTS IN POLYESTER GAS SCRUBBERS
REACTOR FOR CATALYTIC GAS REACTIONS
HAMPNH65EEA
HUEGG 67PCG
BLOCK CATALYST USED IN THE CATALYTIC REACTIONS IN THE GAS
PHASE
CATALYTIC APPARATUS
FOR GAS REACTIONS
KINETICS OF SORPTION AND OF THE CHEMICAL REACTION ON A
UNIFORM-SURFACE CATALYST IN A FLUIDIZED BED tNVOLV
COMPLETE INTERMIXING OF PARTICLES AND OF THE GAS
INST 67BCU
JAEGA078CAF
PRODUCTION OF SUFURIC-ACID AND OXIDE FROM GAS PUR
MALTR 63ROS
CATALYTIC OXIDATIONS IN THE GAS PHASE MARTEA46COI
GAS ABSORPTION APPARATUS MELLRA6AGAA
TREATMENT OF GAS FOR SULFURIC-ANHYDRIDE MANUFACTURE
MERRHF27TOG
ABSORPTION OF SULFUR-DIOXIDE FROM GAS META 62ASD
SULFUR-TRIOXIDE FROM GAS LOW IN SULFUR-DIOXIDE CONTENT
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AMMONIA PROCESS FOR REMOVAL OF SULFUR-DIOXIDE FRPM FLUF GAS
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PHASE SCHOR 67ACF
76
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GAS
PAGE 42
REGENERATION OF A PLATINUM CATALYST BY OXIDATION ANO
TREATMENT WITH A HYDROGEN-CONTAINING GAS SCHWEF66ROA
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REMOVAL OF S02 FROM GAS MIXTURES
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EFFECT OF'GAS ENVIRONMENT ON CERTAIN SEMICONDUCTOR
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GAS MIXING AND MOVEMENT OF SOLID PARTICLES IN A
FLUIDIZED-BED TRABOG62GMA
CATALYTIC PROPERTY OF VANADIUM-OXIDE IN THE REDUCTION OF
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IMPROVED SULFUR-REACTING MICROCOULOMETRIC CELL FOR
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GAS-PHASE
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GAS-THERMAL-CONOUCTIVITY
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GASEOUS CATALYSIS BY MF.TALS OF THF PLATINUM
CATALYTIC COMBUSTION OF GASECUS IMPURITIES IN WASTE AIR
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78
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10/27/69
GASES
PAGE 44
PROCESS DEVELOPMENT IN REMOVING SULFUR-DIOXIDE FROM HOT
FLUE GASES PILOT PL&NT STUDY OF THE ALKALIZED
ALUMINA SYSTEM FOR SULFUR-DIOXIDE REMOVAL BIEND 67PDP
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10/77/69
GASES
GEL
GLASS-FABRIC
GLASS-WOOL
GOLD
GRAIN
GRAINS
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CLEANING WASTE GASES IN THF DOROGOWILOVSK CHEMICAL PLANT
SCRUBBING AND UTILIZATION OF EXHAUST GASES FROM . ._..
FACTORIES IN THE NORTHERN USSR SHABAP63SUE
REMOVAL OF SULFUR-DIOXIDE FROM OXYGEN CONTAINING GASES
SHEL 66ROS
RFMOVAL OF S02 FROM GASES BY USING VARIOUS GRADES PF
ACTIVATED CARBON SIEDJ &ARSG
PURIFICATION OF COMBUSTION GASES
ELECTROSTATIC DEPOSITION OF SULFURIC-ACID MISTS
WASTE GASES OF SULFUR 1C-AC!0 MANUFACTURE
RECOVERY OF SULFUR-OXIDES FROM STACK GASES
COMPRESSORS WITH HYDRAULIC PISTONS FOR CORROSIVE
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PAGE 47
THE LIMITING CONDITIONS OF THE EXISTENCE OF A GRANULAR
CATALYST BED KURGVM65TLC
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10/27/69
HEAT
HEATER
HEATERS
HEATING
HEATING-UP
HEAVY
HETEROGENEOUS
PAGE
HFAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS II. THE
EFFECT OF CATALYST CONDUCTIVITY ON THE APPARENT
CONDUCTIVITY OF THE CATALYST BED AND THE HEAT TRANSFER
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HEAT AND MASS TRANSFER FOR HETEROGENEOUS CATALYSIS
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HEAT AND'MASS TRANSFER IN HETEROGENEOUS CATALYSIS VII EFFECT
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SULFUR OXIDATION WITH INTERNAL HEAT EXCHANGE PETRNM47SOW
HEAT LOSSES TO THE SURROUNDINGS AND PROCESS STABILITY OF A
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10/27/69
HFTEROGENEOUS
PAGE 49
DIFFUSION PROCESS IN GAS HETEROGENEOUS GAS CATALYSTS
ALOEH 62DPI
ANOMALIES CAUSED BY THE SLOW ADSORPTION OF A REACTANT ON THE
COURSE OF CERTAIN TYPES OF CONSECUTIVE AND BRANCHED
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THE PROBLEM OF EXPERIMENTAL INVESTIGATION OF SEPARATE STAGES
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LINEAR FREE-ENERGY RELATIONSHIPS IN HETEROGENEOUS CATALYSIS
V. AN APPLICATION OF QUANTUM CHEMICAL REACTIVITY INDEXES
TO HETEROGENEOUS CATALYSIS MOCHI 67LFE
THE STRUCTURE ANO ACTIVITY OF 'HETEROGENEOUS CATALYSTS
MOSSRL66SAH
LABORATORY INVESTIGATION OF HETEROGENEOUS CATALYTIC
PROCESSES
SURFACE MODELS IN HETEROGENEOUS CATALYSIS
HETEROGENEOUS OXIDATION REACTIONS
HETEROGENEOUS PROCESSES IN RADIATION CATALYSIS
ADSORPTION EQUILIBRIUMS AND REACTION SEQUENCES
HETEROGENEOUS CATALYTIC REACTIONS
HETEROGENEOUS GAS CATALYSIS AT HIGH TE«PCR1ATURFS
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PARRG &&SMI
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SHERTK650PI
HETEROGENEOUS RADIATION CATALYSIS SPITVI64HRC
HETEROGENEOUS RADIATION CATALYSIS AND RADIOACTIVE CATALYSIS
SPITVI66HRC
SOME OBSERVATIONS ON THE CALCULATION OF HETEROGENEOUS
CATALYSIS VANOC 62SOO
LINEAR FREE-ENERGY RELATIONSHIPS IN HETEROGENEOUS CATALYSIS
IV. REGIONAL ANALYSIS FOR SOLID ACID CATALYSIS
YONEY 67LFE
HETEROGENEOUS CATALYSIS USING A TUBE CATALYST I. NATURE OF
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DETERMINING THE RETARDATION DEGREE OF THE THERMAL
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A B Y Z V M6 7 D T R
CHROMIUM-VANADIUM CATALYST WITH A HIGH VELOCITY CONSTANT
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IMPROVED CATALYST OF HIGH LOAD CAPACITY FOR SULFURIC-ACID
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PREPARATION OF SULFURIC-AC10 WITHOUT A CATALYST AT HIGH
PRESC'JRE BURYKA64PSA
POROUS ACTIVATED ALUMINA OF HIGH MECHANICAL STRENGTH
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THE EFFECT OF HIGH CONCENTRATIONS OF SULFURIC-AC 10 ON THE
OF SULFUR-DIOXIDE IN THE PRESENCE OF
RATE OF OXIDATION
BIVALENT MANGANESE
IONS
KASHLI36TEO
THl'OXlDAtldN OF GASES HIGH IN SULFUR-DIOXIDE AND OXYGEN IN
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HIGH AND LOW-TEMPERATURE MECHANISM
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OF
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REACTIONS ON SEMICONDUCTING OXIDES KRAUA 67HAL
THE OXIDATION OF GASES HIGH IN SULFUR-01 0X1 DE AND OXYGEN IN
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PRODUCTION OF A GAS OF HIGH SULFUR- TRI OXIDE CONTENT
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MANUFACTURE OF AN OXIDATION CATALYSTS FOR USE AT HIGH
TEMPERATURES "OSS 67MOA
HETEROGENEOUS GAS CATALYSIS AT HIGH TEMPERATURES
SELECTIVITY FOR SUCCESSIVE FIRST ORDER REACTION AND CATALYST
PORE STRUCTURE DURING HIGH DIFFUSIVE RESISTANCE PROCESSES
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EFFECT OF HIGH TEMPERATURE PLASTIC DEFORMATION AND
SUBSEQUENT QUENCHING ON THE CORROSION AND MECHANICAL
PROPERTIES OF CHROMIUM NICKEL AUSTENTIC STEELS
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AQUEOUS LIQUIDS OF HIGH OXIDIZING POTENTIAL MINTHA59ALO
EFFECT OF. SILICON ADDITIONS ON THE CORROSION BEHAVIOR OF
HIGH-ALLOY AUSTENTIC STEEL IN SULFUR IC-AC ID SOLUTIONS
THE INFLUENCE OF SOME VARIABLES CHARACTERIZING THE QUENCHING
OF HIGH-FREQUENCY WAVES IN THE OXIDATION OF SULFUR-DIOXIDE
NECHN 35TIO
10/?7/69
HIGH-FREQUENCY
PAGE
51
OXIDATION OF SULFUR-DIOXIDE IN
A HIGH-FRFOUENCY DISCHARGE
ZALON 3300S
POSSIBILITY OF THE INFLUENCE OF LONG WAVES OF A
HIGH-FREQUENCY DISCHARGE ON GASEOUS CHEMICAL REACTIONS
HIGH-TEMPERATURE
PREVENTION OF LOW AND HIGH-TEMPERATURE CORROSION AND
DEPOSITS IN OIL-FIRED STEAM BOILERS BY COMBUSTION
WITH LOW AIR SURPLUS CHATM 66PLH
HIGH-VOLT AGE
HINSHELWOCD
HOMOGENEOUS
HOPCALITF
HOUGEN-WATSON
HYDROCARBON
HYDROCARBONS
MYOROOYNAtMC
HYDRODYNAMICS
UTILIZATION OF HIGH-VOLTAGE ELECTRIC FIELDS FOR THF
DESULFURIZATION OF FLUE-GAS ACS M 66UOH
OXIDATION OF SULFUR-DIOXIDE IN A HIGH-VOLTAGE ARC-DISCHARGE
OXIDATION OF SULFUR-DIOXIDE IN
EFFECT OF INTERNAL DIFFUSION O
EFFECT OF PARTICLE SHAPE ON
HINSHELWOOD TYPE OF KINETICS
A HIGH-VOLTAGE ARC-DISCHARGE5
KOLOLA3400S
SCHNP 66EID
INITIATING A HOMOGENEOUS REACTION IN A GAS BY SOLID CATALYST
THE KINETICS OF THE HOMOGENEOUS GASEOUS OXIOAT I ONBOF°ML*61 *"
SULFUR-DIOXIDE CULLCF66TKO
SEMICONDUCTANCE AND CATALYSIS RELATION BETWEEN
CATALYTIC ACTIVITY STOICHIOMETRIC COMPOSITION AND STATF
OF ELECTRON LINKAGE FOR N-CONDUCTING "IXFD CATALYSTS OF
THE HOPCALITE-TYPE III. RELATION BETWEFN CATALYTIC
ACTIVITY STOICHIOMETRIC COMPOSITION AND RATE OF ELECTRON
LINKAGE FOR P-CONDIJCT ING MIXED CATALYSTS OF THE HOPCALITE
TYPE HIENG 6«AC
THE INTERPRETATION OF INITIAL RATE
HOUGEN-WATSON MODELS
DATA WITH THE USE OF
MEZAR &7Tio
APPLIED HYDROCARBON THERMODYNAMICS HEAT CAPACITY DIFFERENCES
P DM I Uf"& 7 A MM
APPLIED HYDROCARBON THERMODYNAMICS IDEAL GAS STATF
PROPERTIES FDIU1WC67AHT
CATALYST REGENERATION FOR THE CONVFRSION OF HYDROCARBONS
STAN 64CRF
THE HYORnOYNAMIC MODEL OF A FL III DI 7ED-BF.D
ABAEGN64THM
HYDRODYNAMICS AND MASS TRANSFER IN A NOZZLELESS VENTURI
ABSOR3ER ABSORPTION OF SULFUR-DIOXIDE INTO WATER
AND WATER SOLUTIONS OF SURFACE ACTIVE AGENTS
ELEND ftAHMT
THE INFLUENCE C1F SMALL QUANTITIES OF ADOFO PLATIMJM ON THE
gAT*LYnC ACTIViTY_QF VANADIUM-PFNTOXIDE REGARDING THF.
3X1 OAT ION OF HYDROGEN
ILCHNI67TIO
C5
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10/27/69
PAGE 52
HYDROGEN
CHEAP HYDROGEN FOR BASIC CHEMICALS JUDAW 6TCHF
EFFECT OF LOW-COST ELECTROLYTIC HYDROGEN ON THE GENERATION
OF BASIC CHEMICALS JUDAH 67EOL
DIFFERENCE IN THE OXIDATION PROCESSES OF SULFUR-DIOXIDE
AND HYDROGEN ON A PLATINUM CATALYST UNDER THE CONDITIONS
OF CHILLING AND THE APPLICATION OF AN ELECTRIC FIELD
STADPM65DIT
CATALYTIC OXIDATION OF SULFUR-DIOXIDE BY HEAVY HYDROGEN
DN A PLATINUM SPONGE TITAT AOCOS
HEAVY HYDROGEN AND OXYGEN TITAT 52HHA
HYDROGEN-FLOUR IDE
ACTION OF HYDROGEN-FLOUR IDE ON THE VANADIUM-BARIUM CONTACT
MASS FOR THE OXIDATION OF S02 AOAOIE37AOH
HYDROGEN-SULFIDE
EFFECT OF HYOROGEN-SULF IDE AND SULFUR-DIOXIDE ON THE
• CORROSION'OF CHEMICALLY RESISTANT CHROMIUM NICKEL STEEL
IN A SOOIUM-SULFATE SOLUTION ACIDIFIED WITH SULFURIC-ACID
HERBG 66EHS
SIMULTANEOUS ABSORPTION OF HYDROGEN-SULFIDE AND
S02 RY &MMONIUM-SULFITE-BISULFITE SOLUTIONS UNDER
SEMI-COMMERCIAL CONDITIONS - IVAND 64SAH
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SULFIDE ON
COMPLEX SPIRALS OF PLATINIZED NICHROME KOTENZ57COO
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SULFIDE
ON COMPLEX SPIRALS OF PLATINIZED NICHROHE KOTENZ57COS
VISCOSITY AND INTERMOLECULAR POTENTIALS OF HYDROGEN-SULFIDE
SULFUR-DIOXIDE AND AMMONIA PAL AK67VIP
INVESTIGATION OF THE MECHANISM OF OXIDATION HYDROGENATION
AND ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS
OXIDATION OF SULFUR DIOXIDE ON ACTIVATED CARBON AT 20-DEG
IN THE PRESENCE OF HATER VAPOR OAVTOK61IMO
MECHANISM OF OXIDATION HYDROGENATION AND ELECTROCHEMICAL
COMBUSTION ON SOLID CATALYSTS CATALYTIC PECULIARITIES
OF SURFACE OXIDES ON CARBON OAVTOK61NOH
THE MECHANISMS OF OXIDATION HYOROGENATION AND
ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS RELATION
BETWEEN DEPOLARIZING OXIDES ADSORBED ON CARBON AND
PLATINUM AND THE CATALYTIC ACTIVITY IN THE OXIDATION OF
SULFUR-DIOXIDE DAVTOK61TMO
COLLOIDAL CLAY AS CATALYST IN OXIDATION AND HYOROGENATI ON
HAY JG20CCA
_ .CHEMICAL
. _ _ _ . _ LOW TEMPERATURE
OXIDATION ON PLATINUM. OVCHEN61MOO
THE MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE INFLUENCE OF TEMPERATURE AND TIME OF CARBON
DESORPTION ON ADSORPTION AND OXIDATION OF H2S AND S02
SIEflJ 64MCO
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THF CONCENTRATION OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND S02 OXIDATION
PROCESSES SIEOJ 6AMCO
HYDROGENATION
MECHANISM OF OXIDATION HYDROGENATION AND ELECTROCHEM1C
COMBUSTION ON SOLID CATALYSTS
H2S
10/27/69
H7S04
I-S/R
IDEAL-GASES
IGNITION
INDUSTRIAL
PAGE
53
COMPLETION OF THE OXIDATION OF S02 CATALYST FURNACE OF A NEW
TYPE IN A H2SO4 PLANT ALMAG 63COT
THE RECOVERY OF H2S04 FROM WASTE GASES DIMID 65TRO
OXIDATION OF S02 IN AN APPARATUS WITH A FLUIDIZED-BED OF FE-
OXIDE CATALYST DURING H2S04 PRODUCTION BY THE CONTACT
PROCESS LASTYV6600S
HEAT LOSSES TO THE SURROUNDINGS AND PROCESS STABILITY OF A
CONTACT-TYPE H2S04 PLANT i>ETRNMfc6HLT
THE T-S/R AND I-S/R DIAGRAMS FOR IDEAL-GASES FISCS 66TTS
THE T-S/R AND I-S/R DIAGRAMS FOR IDEAL-GASES FISCS 66TTS
THE IGNITION TEMPERATURE OF A WEAR RESISTANT VANADIUM
CATALYST FOR THE OXIDATION OF SULFUR-DIOXIDE
CHERMA65TIT
SEARCH FOR CATALYSTS FOR THE OXIDATION OF SULFUR-DIOXIDE
WITH A DECREASED IGNITION TEMPERATURE GERBEV63SFC
CONVERSION OF SULFUR-DIOXIDE WITH LOW IGNITION CATALYSTS
MANDBG66COS
THE IGNITION TEMPERATURES OF VANADIUM CATALYSTS
THERMOGRAPHIC DETERMINATION OF THE
VANADIUM CATALYSTS
INDUSTRIAL .
DIFFERENT
EFFECTIVENESS
I STRUCTURES
MANUFACTURING CONCENTRATED
PAVLM- 60ITV
IGNITION TEMPERATURE FOR
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WASTE GASES BY THE AMMONIUM CYCLIC METHOD
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3E ITS CHEMISTRY AND REMOVAL FROM INDUSTRIAL
BIEND 58SDC
DAMAGING OF PT CATALYSTS IN INDUSTRIAL USE BLUMH 6600P
SUPPORTED PLATINUM METAL CATALYSTS THEIR SELECTION AND
METHODS OF USE IN INDUSTRIAL PROCESSES BONDGC65SPM
OPTIMIZATION OF CATALYTIC PROCESSES IN INDUSTRIAL REACTORS
BOREGK6000C
THEORETICAL SELECTION PREPARATION AND USE OF INDUSTRIAL
CATALYSTS BORFGK64TSR
SOLUTION TO THE S02 PROBLEM IN AIR PURIFICATION BY
OPERATIONAL AND INDUSTRIAL MEASURES BRC1KW 6ftSTT
KINETIC STUDIES ON THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYSTS III. A COMPARISON OF THF. »ATF. EQUATIONS
OBTAINED WITH SOME INDUSTRIAL VANADIUM CATALYSTS
CHANMC5QKSO
A STUDY ON INDUSTRIAL PREPARATION OF AMMONIUM-SULFATE
BY NONCATALYTIC OXIDATION CHUNKY66SIP
FIXATION AND RECOVERY AS AMMONIUM-SULFATE DF WASTE
DIOXIDE IN INDUSTRIAL EFFLUENT GAS Cl 117J 65FAR
RECOVERY OF SULFUR-DIOXIDE FROM INDUSTRIAL GASES
FMPP f>7ROS
INSTALLATIONS FOR INDUSTRIAL GAS CLEANING PROCESS
OPTIMIZATION FOR OPERATING MULTIPLE INSTALLATIONS IN ANY
REGIME FERPG
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10/27/69
INDUSTRIAL
INDUSTRV
RECOVERY OF SULFUR FROM INDUSTRIAL GASES
PAGE 54
FIVE 66ROS
SULFUR-DIOXIDE REMOVAL FROM INDUSTRIAL'HASTE-GASES IN PILOT
CALE PLANTS HE|NG
AND FULL
OR OXIDATION OF AUTOMOBILE AND INDUSTRIAL FUME
SANITARY REMOVAL OF SULFUR-DIOXIDES FROM INDUSTRIAL GASES
KLIMR 64!
IN INDUSTRIAL
ES
KEITC065ACF
AL GASES
KLIMR 64SRS
USE OF CERTAIN CATALYSTS AND ADSORBENTS
HYGIENE PRACTICE AND IN PRODUCTION KOTENZ66UOC
THE RATE OF OXIDATION OF S02 WITH INDUSTRIAL VANADIUM
CATALYST KUBOH 59TRO
ATTEMPTS TO INCREASE THE THERMAL RESISTANCE OF THE
INDUSTRIAL VANADIUM CATALYST IN THE REACTION OF OXIDATION
OF S02 KUCZH S9ATI
CERTAIN PRINCIPLES OF THE MOTION OF CATALYST PARTICLES IN
INDUSTRIAL VERTICAL ^PNEUMATIC CONVEYING KURGVM66
PURIFI --------
IAL VERTICAL ^PNEUMAT
ION OF INDUSTRIAL GASES FROM
CONVEYING
SULFUR-DIOXIDE
&6CPM
PURIFICATION OF INDUSTRIAL EXHAUST GASES
KINETICS OF SULFUR-DIOXIDE OXIDATION ON AN INDUSTRIAL
KUZN1E66P1G
OI
MALAJ 6TPO
VANADIUM CATALYST
INDUSTRIAL HASTE-GAS PURIFICATION
REMOVAL OF SULFUR-OXIDES FROM INDUSTRIAL GASES
REMOVAL OF SULFUR-DIOXIDE FROM INDUSTRIAL GASES
THE SIMULTA
REDUCED f
FLUE-GASI
NEOUS ABSORPTION OF SULFUR-OXIDES AND ONE OR MORI
ULFUR COMPOUNDS FROM INDUSTRIAL GASES ESPECIALLY
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PERFORMANCE OF AN INDUSTRIAL APPARATUS FOR
"- 'N A FLUIDIZED CATALYST BED
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S02 IN A FLUIDIZED CATALYST BE
CATALYTIC COMBUSTION OF
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FUR-TRIPXIDE ADAOIE34UWF
CARS
USEUOFUMANGANESEECATALYSTS IN CHEMICAL INDUSTRY
AUTOMATION OF CONTACT REACTORS IN
CHAGVT65UOM
THE CHEMICAL INDUSTRY
EDSTJ067SDC
PULP MILL
-- TRAR
PREPARATION OF VANADIUM-BASE CATALYSTS FOR THE
STEELSSFOR DIFFICULT CORROSION CASES IN THE CHEMICAL
INDUSTRY EDS
REMOVAL AND RECOVERY OF SULFUR-DIOXIDE IN THE PULP
INDUSTRY GA
UTILIZATION OF DILUTE ADSORPTION CATALYSTS IN THE ~
""r HIMNEYS PIERRR66
IIC HASTES IN THE CHEMICAL INDUSTRY
TECHNICAL PROGRESS AND ECONOMICS OF THE COPPER I NO
SHAKAKooT PA
10/27/69
INDUSTRY
INFRARED
INORGANIC
ION-EXCHANGE
ION-EXCHANGERS
IONIZING
IRIDIUH
IRON
I"ON< MI)
IRON-COPPER
IRON-OXIDE
PAGE 55
AIR-POLLUTION PROBLEMS OF THE PHOSPHATE INDUSTRY
FORMATION OF SULFUR-TRIDXIOE APPLICATION OF INFRARED
SPECTROMETRY TO FUNDAMENTAL STUDIES
IN
SMITRI68APP
RED
LADNUR63FRT
CHEMICAL EOUIL IRRIA .
PHYSIOCHEMICAL FORCES
INORGANIC SYSTEMS EQUILIBRIUM OF
j IN A CRYSTAL LATTICE KAPUAF36CEU
EXPERIMENTAL LOCAL PURIFICATION OF HARMFUL ORGANIC AND
INORGANIC DISCHARGES INTO THE ATMOSPHERE AW INTO BODIES
OF HATER ROSCSE66ELP
REMOVING INORGANIC HASTES IN THE CHEMICAL INDUSTRY
SCHEC 64RIH
ABSORBING SULFUR-DIOXIDE ON DRV ION-EXCHANGE ROSINS
COLFR 60ASD
CATALYSTS RASED ON ION-EXCHANGERS
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EFFECT OF IONIZING RADIATIONS ON THF SULFIIK-r)| nx 1DF-DXYC.EN
SYSTEM II THE OXIDATION OF SULFUROUS-AC I 0 TO SULFUR IC-AC ID
BY ACTION OF X-RAY RAOIATION SCHRR 64EOI
DELETERIOUS ACTION OF RHODIUM AND OF IRIOIUM UPON PLATINUM
IN THE CATALYSIS OF SULFUR 1C -ANHYORI OE LFVIGR270AO
USE OF AN IRON CATALYST IN THE CONTACT CHAMBER PROCESS
ESFLIM64UOA
PROTECTION OF IRON »OWOE« BY THE LEAO-AZELATE
REMOVING IRON FROM DEACTIVATED OIL TREATMENT CATALYSTS
CONTAINING PLATINUM LFDPJC.65RIF
PURIFICATION OF SULFURIC-ACID IRON CONTAINING HASHING
DISCHARGES MATAVL87PSA
EFFECT OF HATER VAPOR AND IRON COMPOUNDS ON THE ACTIVITY
OF VANADIUM CATALYSTS IN A FLUIDI ZED-BED MUKHIP63EOH
A MECHANICALLY STABLE IRON CATALYST FOR THE OXIDATION OF
SULFUR-DIOXIDE MUKHIP64AMS
THE CORROSION RATE OF CAST IRON BY SULFUR-DIOXIDE
MAKING ACID IN IRON AND STEEL EQUIPMENT RINCJR67MAI
STUDY OF CORROSION OF IRON AND ITS ALLOYS IN CHLORINE AND
SULFUR-DIOXIDE BY THE THERMOGRAPH 1C METHOD TDVMIK66SCI
OXIDIZING SULFUR-DIOXIDE BY USING FLUIDIZFD IPONIIIII OXIDE
BlICT 610SD
THF CATALYTIC PROPERTIES CF NDNPL4TINU» CATALYSTS IN THE
OXIDATION OF SULFUR-niOXIOE TO SULFUR-TRIOXIDE THE
ACTIVITY OF IRON-COPPER CATALYSTS KURINP43TCP
THE PREPARATION OF HEAR BESISTANT IRON-OXIDE CATALYST
nfWKE!f>6TPO
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10/27/69
I RON-OX IDE
IRRADIATION
ISOTHERMS
ISOTOPE
KACHKAROFF
KIESELSUHR
KINETIC
KINETICS
PAGE
SPECTROGRAPHIC AND X-RAY DIFFRACTION STUDY OF IRON-DXIDE
£»!aLY.ST FOR..SULFUR IC-AC ID MANUFACTURE.
56
INTERACTIONS IN SULFUR-
_ .. ._
IRON-OXIDE SYSTEMS
SULFORIC-ACID CATALYSIS WITH IPON-OXIDE
LEVYA 67ISO
NEUMB 37SAC
INVERS MIXED CATALYSTS SULFUR-TRIOXIDE SYNTHESIS USING
IRON-OXIDE CATALYST ON A SILVER CARRIER SCHHGM67IMC
CATALYSIS UNDER IRRADIATION IN THF PRESENCE OF NONMETALLIC
SOLIDS COEKR 63CUI
EFFECTS OF X-RAY IRRADIATION ON THE OXIDATION OF
SULFUR-DIOXIDE BY V4NAD I A-TI TANI A CATALYSTS
KUBOT 57EOX
A S-TUDY- OF ADSORPTION ISOTHERMS ON OXIDE FORMS OF
METALSIL ICATE CARRIERS AND CATALYSTS
ZULFZG66SAI
ISOTOPE EFFECT OF SULFUR DURING THE OXIDATION OF
S02 IN SULFUR1C-AC1D AND THE MECHANISM OF THIS
OXIDATION COURP 65IES
ISOTOPE EXCHANGE FOR THE OXYGEN OF VANADIUM-PENTOXIDE WITH
SULFUR-DIOXIDE AND TRIOXIDE KASALA64IEF
S02 CONVERSION IN THE KACHKAROFF PROCESS
SANDO 63SCI
REGULATION OF POROSITY AND MECHANICAL STRENGTH OF SHAPED
KIESELGUHR CATALYST CARRIERS • JELIJF65RPM
SURFACE STRUCTURE OF'KIESFLGUHR CARRIERS AND CATALYSTS FOR
THE OXIDATION OF SULFUR-DIOXIDE JIRUP 57SSO
THE MECHANISM OF THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
WITH A COMMERCIAL VANADIUM CATALYST A KINETIC STUDY
CALDPH52TMO
KINETIC STUDIES ON THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYST" "- ' ~
III. A COMPARISON OF THE RATE EQUATIONS
OBTAINED WITH SOME INDUSTRIAL VANADIUM CATALYSTS
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SOME PARAMETER ESTIMATION CONSIDERATIONS FOR HETEROGENEOUS
KINETIC MODELS MF7AR 66S"E
EFFECTIVENESS FACTOR F01 POROUS CATALYSTS LANGMUIR-H1NSHEL
WOOD KINETIC EXPRESSIONS R08EGW65EFF
KINETIC ANOMALY OF CATALYTIC CONTACT REACTIONS IN A
FLUIOIZED LAYER DF SMALL DIMENSIONS SZOLP 62KAO
KINETIC STUDIES OF THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYSTS PROMOTED BY ALKALI 1ETAL SALTS
7AKHMS5BKSO
EQUILIBRIUM POSITION AND KINETICS OF OXIDATION OF
SULFUR-DIOXIDE AND SYNTHESIS OF AMMONIA ANDRL ME»A
ASPECTS OF THE KINETICS OF FAST CATALYTIC
REACTION KINETICS IN A TUBULAR REACTOR
THE NATURE HF BAUR'S KINETICS
REACTIONS
ANDBL 67AOT
BARPT 52RKI
BAURE 44TNO
10/27/69
KINETICS
PAGE
57
THE KINETICS OF THE OXIDATION OF SULFUR-DIOXIDE BY
NITROUS-OXIDE BFLLTN55TKO
THE KINETICS OF THE CONTACT OXIDATION OF SULFUR-DIOXIDE
BOREGK33TKO
KINETICS OF CONTACT OXIDATION OF SULFUR-DIOXIDE IN THE
PRESENCE OF FERRIC-OXIDE BOREGK44KOC
KINETICS OF THE CONTACT SYNTHESIS OF SULFURIC-ACID
BOREGK45KOT
KINETICS OF REVERSIBLE CATALYTIC REACTIONS IN THE INTERNAL
DIFFUSION RANGE BOREGK52KOR
THE KINETICS OF SULFUR-DIOXIDE OXIDATION OVER VANADIUM
CATALYSIS BOREGK67TKO
KINETICS OF THE OXIDATION OF SULFUR-DIOXIDE BRODKI41KOT
THE KINETICS OF THE HOMOGENEOUS GASEOUS OXIDATION OF
SULFUR-DIOXIDE CULLCF66TKO
KINETICS OF THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
OAVIB 64KCO
KINETICS OF THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
DAVIS 64KOT
KINETICS OF THE OXIDATION OF SULFUP-DIOXI DE WITH A POISONED
ifERCIAL VANADIUM CATALYST ISHIT 65K
COMME
5KOT
KINETICS OF ACID FORMATION ITKIDY52KDA
THE KINETICS OF OXIDATION OF GASEOUS SULFUR-DIOXIDE IN
AQUEOUS SOLUTIONS AND POISONING OF MANGANIC-SULFATE BY
PHENOL KASHLI35TKO
THEORY OF THE CHAMBER-PROCESS MECHANISM AND THE KINETICS OF
KUZMIN36TOT
KINETICS OF SORPTION AND OF THE CHEMICAL REACTION ON A
UNIFORM-SURFACE CATALYST IN A FLUIDIZED RED INVOLVING
COMPLETE INTERMIXING OF PARTICLES AND OF THE GAS
LAVOKP64KOS
KINETICS FOR REACTIONS OF HETEROGENEOUS CATALYSIS
MAGYM 6*KFR
THE MECHANISM AND THE KINETICS OF SULFUR-DIOXIDE OXIDATION
ON CATALYSTS CONTAINING VANADIUM AND ALKALI OXIDES
MARSP 6RTMA
KINETICS OF SULFUR-DIOXIDE OXIDATION ON AN INDUSTRIAL
VANADIUM CATALYST MICHJ 67KOS
THE KINETICS OF REACTION BETWEEN OXYGEN ATOMS AND
S02 AN INVESTIGATION BY ELECTRON-SPIN-RESONANCE
SPECTROMFTRV MULCMF67KRO
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DIFFERENTIAL CHROMATOGRAPH1C METHOD OF STUDYING THE
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INVESTIGATION BY THE DIAPHRAM METHOD ROITVA58EOT
THE KINETICS OF OXIDATION OF SULFUR-DIOXIDE ON A PLATINUM
CATALYST UNDER EQUILIBRIUM CONDITIONS ROITVAbOTKP
INVESTIGATION OF THE KINETICS OF THE PROCESS(S02+.Sn2=SO3»
IN THE STATE OF CHEMICAL EQUILIBRIUM ON A'PT CATALYST BY
THE AID OF RADIOACTIVE S ROITVA6ZIKP
THE EFFECT OF CATALYSTS AND ANT1CATALYSTS ON THE KINETICS
AND MECHANISM OF THE OXIDATION OF SULFUR-DIOXIDE
RUIZVP36TEO
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KINET ICS
LANGMUIR
PAGE 58
KINETICS OF THE CATALYTIC FORMATION OF SULFURIC-ACIO ON A
BAR1UM-ALUMINUM-VANADIUM CATALYSTS RZAFPBfrOKOT
EFFECT OF INTERNAL DIFFUSION ON CATALYTIC REACTIONS
EFFECT OF PARTICLE SHAPE ON REACTION WITH LANGMUIR
HINSHELWOOO TYPE OF KINETICS SCHNP 66EIO
KINETICS OF SULFUR-DIOXIDE OXIDATION ON VANADIUM-PENTOXIDE
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KINETICS OF THE OXIDATION OF SO? IN A FLUIDIZFD CATALYST (JED
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THE KINETICS OF THE OXIDATION OF SULFUP-DIOXIDE SOLUTIONS
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KINETICS OF REGENERATION OF SPHERICAL CATALYST IMMOBILE
LAYER ZHORYM67KRS
EFFECT OF INTERNAL DIFFUSION ON CATALYTIC REACTIONS
EFFECT OF PARTICLE SHAPF ON REACTION WITH LANGMUIR
HINSHELWOOD TYPE OF KINETICS SCHNP 65EID
LANTHANIOE-GROUP
PROMOTING ACTION OF GROUP-I AND THE LANTHANIDE-GROUP
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EQUILIBRIUM OF
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PHYSIOCHEMICAL FORCES IN A CRYSTAL LATTICE KAPUAF36CEU
DETERMINATION OF THE SPEED OF CONVERSION OF SULFUR-DIOXIDE
TO SULFUR-TRIOXIDE ON PASSING THROUGH A CATALYTIC LATTICE
SANSJ 3AOSC
METHOD FOR REGENERATION OF LEAD CONTAMINATED CATALYSTS
MICHE 67MRL
CORROSION OF LEAD ALLOYS IN SULFURIC-ACIO "ELZVE67CLA
PROTECTION OF IRON POWDER BY THE LEAO-AZELATE
KORMNA66PIP
USE OF GRAPHITE BLOCKS FOR PROTECTION OF SCRUBBING TOWERS
IN THE SULFURIC-ACID PLANT OF UST-KAMENOGORSK LEAD-ZINC
COMBINE
THE OXIDATION OF SULFUR-DIOXIDE
"EREYP67UGB
IN ULTRA-VIOLET LIGHT
KORNG 31TOO
LIMESTONE MILL DRYING PLANTS FOP THF REMOVAL OF
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ABSORPTION OF SULFUR-DIOXIDE AND SEPARATION OF ASHFS FROM
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LYF AXELK06MSD
OPTIMUM CONDITIONS OF MAGNESITF REMOVAL (IF SULFUR-DIOXIDE
FROM EXHAUST-GASES
10/?7/6
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MANUFACTURE
MANUFACTURED
MANUFACTURING
MASS
PAGE f.c
THE MANUFACTURE OF $IIL Fi|P I C.-AC I D BY MEANS OF VANAOIU"
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DRAFT RESISTANCF IN A S.1JM_L CQNVFK.TER OSAMG 31TMO
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MANUFACTURE OF SULFUR FROM GAS CONTAINING SULFUR-DIOXIDE
f)Y 0 67MSF
PRODUCT ION OF dLFll" IN THE MANUFACTURE "F SULFUR IC-ACI0 BY
THF SHHRTENFD CONTACT PROCESS
SULFURIC-ACID MANUFACTURE
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DETERMINATION OF THE DEGREE OF OXIDATION OF SULFUR-DIOXIDE
IN THE MANUFACTURE OF SULFUPIC-ACID SOCIET560DO
ELECTROSTATIC DEPOSITION OF SULFURIC-ACID MISTS FROM THE
WASTE GASES OF SULFUR1C-ACID MANUFACTURE STOP* hSEDS
MANUFACTURF OF SOLID CATALYSTS UCHIH 67MSC
PROCESS FDR EXTRACT I ON'OF V9LUARLE PRODUCTS FPOM SCHISTS
AND OTHE" BITUMINOUS FE"RUNG I NOUS AND SULFUOOUS SEDIMENTS
AND COMPOUNDS MANUFACTURED THFREFRQM LUPAK 66PEV
MANUFACTURING CONCFNTRATEO SULFIIR-OIOX IDE FROM INDUSTRIAL
WASTE GASES BY THE AMVONIUM CYCLIC METHOD BETTJ 65MCS
MANUFACTURING UP TO 60 PER CENT OLEUM OP SULFURIC-ACID
THE USE OF CONTACT EO'IIPNENT WITH A FLUIDIZED CATALYST RED
IN THE MANUFACTURING HF SULFUPIC-ACID MUKHIP63TUO
RECOVERY OF VANADIUM FROM THE SPENT V-K SILICA GEL CATALYST
USED IN PHTHAL 1C-ANHYDRIDE MANUFACTURING SHESAPhSROV
INFLUENCE OF THE COMPOSITION AND THE DISTRIBUTION OF THE
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ACTION OF HYDROGEN-FLOUR IDE ON THE VANADIUM-BARIUM CONTACT
MASS FOR THE OXIDATION OF SO? AOADIE37AOH
MASS TRANSFER COEFFICIENTS DURING THE ABSORPTION OF S02
FROM GASES BY iMIUNIUM-SULFITE-BISUlFITE SOLUTIONS^
MASS TRANSPORT AND CHEMICAL REACTION IN MULTIFUNCTIONAL
CATALYST SYSTEMS DUNNDJ6SMTA
FILTER MASS FOP THE REMOVAL (IF SUI FUR-OIPXI DE FROM WASTE
GASES cHKtW 66FMR
HYDRODYNAMICS AND MASS TRANSFER IN A NOZ7LELESS VFNTURI
ABSORBER A»snR°TldN PF SUI.F UR-OIOXIDE INTO WATER
AND WATER SOLUTIOVS OF SURFAfh ACTIVE AGENTS
IMPROVEMENT OF THf MASS TRANSI'iil I"11M 4 i"iAS TO A POROUS
CATALYST OP ADSOR«e\T HY PRt- <«SllKr nsClLLATIONS
IO/?7/69
MASS
MASS-ACTION
MASSES
MATERIAL
MATERIALS
PARE
61
HEAT AND MASS TRANSFER IN CATALYTIC BEOS FROMGF66HAM
MASS SPECTROMFTRY OF MATERIALS PRODUCING SULFUR-TRI OXI DE
MODELLING OF CHEMICAL REACTORS HEAT AND MASS TRANSFERRWITHIN
A POROUS CATALYST PARTICLE SOME RESULTS OF AN ANALYSIS
FOR A ZERO-ORDER REACTION HLAVV 67MOC
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS II. THE
EFFECT OF CATALYST CONDUCTIVITY ON THE APPARENT
CONDUCTIVITY OF THE CATALYST BEO AND THE HEAT TRANSFER
COEFFICIENT FROM THE BED TO REACTOR BATH HORAJ 67HAM
OVERALL CATALYTIC EFFECTIVENESS FACTORS AND THEIR SHAPF
CORRELATIONS WITH MASS TRANSFER AND REACTION ON THF
EXTERNAL SURFACE KASAS 67OCE
MASS TRANSFER IN A SCRUBBER WITH CONE-SHAPED GRID PLATES
KH OK S FA *5 M T ^
HEAT AND MASS TRANSFER FOR HETEROGENEOUS CATALYSIS
HEAT AND MASS TRANSFER IN HETEROGENEOUS C ATALYS1
OF CATALYST HEAT CONDUCT I VITY ON THE OVFRALL HEAT
TRANSFER COEFFICIENT IN A PACKED TUBE MAMUP 67HAM
MODELLING OF CHEMICAL REACTORS vi. HEAT AND MASS TRANSFER
IN A POROUS CATALYST "ARTICLE THE MULTIPLICITY OF SOLUTION
FOR THE CASE OF AN EXOTHFRMIC ZERO-ORDER REACTION
MASS TRANSFER AND ABSORPTION WITH REACTION IN ROTARY6" 68MOC
TY«»E EQUIPMENT
MASS AND HEAT TRANSFER
IN r.AS-SOLin SYSTEM
NIKON 66MTA
WICKE 51MAH
THE LAW OF MASS-ACTION AS THE BASIS FOR CALCULATING THE BEST
YIELD FROM TECHNICAL AND ECONOMIC STANDPOINTS
SAVEW S?TLO
CATALYTIC MASSES SUCH AS THOSE SUITABLE FOR OXIDIZING
SULFUR-DIOXIDE TO TRIO* IDE CONNGC28CHS
CONTACT MASSES FOR HETEROGENEOUS GAS CATALYSIS
VANADIUM CATALYTIC MASSES IN MANUFACTURE OF SULFUR*C-ACI tf**
KRUME MVCM
SELECTION OF MATER IlAL FHR CONT« T CATALYSTS
_. AL FDR CONTACT CATALY
PROPERTIES OF SEMICONOVIC TING CATALYSTS"
BEHAVIOR AND
MATERIAL AND HEAT 1NG~BALANCE CALCULATIONS IN CHEMICAL"* S6SOM
TECHNOLOGY GELEH 66MAH
PREHEATING A CATALYTIC REACTOR BY DIRECT FEED OF FUEL GASES
TO THE CATALYST MATERIAL OSMUVA64PAC
REGENERATION OF A SULFUR-DIOXIDE ABSORBER MATERIAL
REGENERATION OF CONTACT MATERIAL VANLJ 6SRCM
NEW CONSTRUCTION MATERIALS FOR APPARATUS IN SULFUR1C-AC1D
AND SELENIUM PRODUCTION BIILYI Y£?NrM
* COMPUTATIONAL .MODEL F"R THE STRUCTURE OF POROUS MATERIALS
FHSTRN66ACM
COMPUTATIONAL MODEL
EMPLOYED IN CATALYSIS
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10/27/69
MATERIALS
MATHEMATICAL
MECHANICAL
MECHANICALLY
MECHANISM
PAGE
MASS SPECTRQMETRY OF MATERIALS PRODUCING SULFUR-TRIOXIDE
GOHLRS66MSM
THE CHOICE OF RAW MATERIALS FOR THE MANUFACTURE OF
SULFURIC-ACID HEIDM 67TCO
ACCELERATING CATALYTIC REACTIONS BY RAPID MOVEMENT OF THE
MATERIALS KIPPHB19ACR
ACCELERATING CATALYTIC REACTIONS BY RAPID MOVEMENT OF THE
MATERIALS KIPPHR24ACR
CORROSION BEHAVIOR OF SOME METALLIC MATERIALS IN LIQUID
SULFUR-DIOXIDE RIVOL 66CBS
CONSTRUCTION MATERIALS FOR FILTERING APPARATUS IN
NICKEL COBALT PRODUCTION SHVAGL63CMF
MATHEMATICAL MODEL OF CATALYTIC REACTORS GENERAL PRINCIPLES
CYBUA 67MMC
MATHEMATICAL MODELS OF CATALYTIC REACTORS HEAT AND MASS
TRANSFER CYBUA f>7NMO
MATHEMATICAL DESCRIPTION OF THE OXIDATION OF SULFUR-DIOXIDE
INTO SULFUR-TRIOXIOE DURING MET CATALYSIS KARTMB66MOO
POROUS ACTIVATED ALUMINA OF HIGH MECHANICAL STRENGTH
HUTTJC65PAA
REGULATION Of POROSITY AND MECHANICAL STRENGTH OF SHAPED
KIESELGUHR CATALYST CARRIERS JELIJF65RPM
INCREASING THE MECHANICAL STRENGTH OF POROUS DISPERSE BODIES
ADSORBENTS AND CATALYSTS RERIPA6*IMS
VANADIUM CATALYST USED IN THE OXIDATION OF S02 EFFECT OF
MECHANICAL TREATMENT OF CARRIER ON THE ACTIVITY OF CONTACT '
SWINA 66VCU
EFFECT OF HIGH TEMPERATURE PLASTIC DEFORMATION AND
SUBSEQUENT QUENCHING ON THE CORROSION AND MECHANICAL
PROPERTIES OF CHROMIUM NICKEL AUSTENTIC STEELS
A MECHANICALLY STABLE IRON CATALYST FOR THE OXIDATION OF
SULFUR-DIOXIDE MUKHIP64AMS
THE EFFECT OF THF CONCENTRATIONS OP IMPREGNATING SOLUTIONS
UPON THE CHEMICAL COMPOSITION AN1 STRUCTURE OF A •
MECHANICALLY STABLE VANADIUM CATALYST MUKHIP65TEO I
S02 OXIDATION ON MECHANICALLY ACTIVATED V205 PAUDR 65SOO
POSSIBLE MECHANISM OF
ON THE CATALYTIC
-. THE EFFECT OF RADIOACTIVE ADDITIONS
. . .... _. ..... AND CHEMISORPTIVE PKO»E".TI F= S OF
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THE "ECHANISM OF THE ELECTROLYTIC OXIDATION OF
BOGOGASBTMO
ULFUR-DIOXIDE IN THE OOF.SFNCF
SULFUR-DIOXIDE
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OF ACTIVATED VANADIUM CATALYSTS
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OF ACTIVATED VANADIUM CATALYSTS STABILITY OF VANADIUM
CQMDiiuNiis UNOtR PIT: CONDITION OF SULFURIC-ACIO CATALYSIS
57
10/27/69
MECHANISM
PAGE
63
MECHANISM OF ACTION OF SOLID CATALYSTS
THE MECHANISM OF THE CATALYTIC OXIDATION OF _..
WITH A COMMERCIAL VANADIUM CATALYST A KINETIC STUDY
BOREGK56MOA
SULFUR-DIOXIDE
CALDPH52TMO
FUSION
LOSS Of PT02 FROM HEATED PT A BOUNDARY LAYER DIP
MECHANISM CHASJC66LOP
INVESTIGATION OF THE MECHANISM OF OXIDATION HYOROGENATION
AND ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS
OXIDATION OF SULFUR DIOXIDE ON ACTIVATED CARBON AT ?0-DEG
IN THE PRESENCE OF WATER VAPOR DAVTOK61IMO
MECHANISM OF OXIDATION HYOROGENAT1 ON AND ELECTROCHEMICAL
COMBUSTION ON SOLID CATALYSTS CATALYTIC PECULIARITIES
OF SURFACE OXIDES ON CARBON DAVTOK61MOH
A NEW MECHANISM FOR THE ACTION OF THE VANADIUM-PENTOXIDE
SILICA-ALKALI PYROSULFATE CATALYST FOR THE OXIDATION
OF SULFUR-DIOXIDE FRAZJH&OANM
MECHANISM OF THE CATALYTIC OXIDATION flF SULFUR-DIOXIDE IN A
SOLUTION OF MANGANESE SALTS GRODMK35MOT
MECHANISM FOR RECOVERY OF PLATINUM LOSSES DURING AMMONIA
CATALYTIC OXIDATION JANIW 67MFR
MFCHANISM OF THE OXIDATION OF SULFUR-DIOXIDE
DETERMINATION OF THE STOICHIONETRIC NUMBER BY MEANS OF S35
KANEY ftSMOS
MECHANISM OF INHIBITING ACTION KASHLI54MOI
MECHANISM OF THE CATALYTIC OXIDATION OF S02 CONSIDERED
FROM THE THEORY OF SEMICONDUCTOR CORRECTION OF THE
MECHANISM OF CALDERRANK KAWAT 54TPP
MECHANISM OF CATALYSIS VALENCE AND ENERGY FORMS OF
HETEROGENEOUS AND ENZYMIC CATALYSIS KOBONIftOMOC
CHEMISORPTION AND MECHANISM OF CATALYTIC REACTIONS ON OXIDE
CATALYSTS KRAUA 62CAM
THEORY OF THE CHAMBER-PROCESS MECHANISM AND THE KINETICS OF
KUZMIN36TOT
THE MECHANISM OF SOLID CATALYSTS WITH SPECIAL REFERENCES TO
SEMICONDUCTOR CATALYSTS MAKIS 57TMO
DEVELOPMENT OF CONCEPTS ON REACTION MECHANISM OF
SULFURIC-ACID PRODUCTION MALIIK66DDC
GENERAL MECHANISM OF CATALYTIC REACTIONS MARSJMft7GMO
THE MECHANISM OF THE OXIDATION OF SULFUR-DIOXIDE ON
POTASSIUM-VANAOIUM-OXIDE CATALYSTS MARSP 64TMO
THE MECHANISM AND THF KINETICS OF SULFUR-DIOXIDE OXIDATION
ON CATALYSTS CONTAINING VANADIUM AND ALKALI OXIDFS
MARSP 68TMA
THE REACTION MECHANISM IN THF CONTACT SULFURIC-ACID PROCESS
AND THE METHOD OF ACTION OF ACTIVATORS NEIJMB 29TRM
MECHANISM OF OXIDATION HYDROGENATION AND ELECTROCHEMICAL
COMBUSTION ON SOLID CATALYSTS LOW TEMPERATURF
OXIDATION ON PLATINUM OVCHEN61MOP
THF MECHANISM OF SULFUR-DIOXIDE OXIDATION IN THE PRESENCE OF
VANADIUM CATALYSTS POLYM 34TMO
THF. MECHANISM OF OXIDATION CATALYSIS BY METAL-OXIDES
RDITVA60TMO
THE EFFECT OF CATALYSTS AND ANTlCATALYSTS ON THE KINETICS
AND MECHANISM OF THF OXIDATION OF SULFUR-DIOXIDE
RUIZVP36TEO
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MECHANISM
MECHANISMS
MERCURY
METAL
PAGE 64
THE ELECTRONIC MECHANISM OF THE CATALYTIC FORMATION OF S03
SCHWGM63EMC
ION ON CR203
ELECTRONIC MECHANISM OF THE CATALYTIC S03 FORMATIt
CONTACTS SCHWGM64EMC
MECHANISM OF ELECTROOXIDAT ION OF SOME COMPOUNDS ON PLATINUM
THE MECHANISM OF CATALYTIC OXIDATION ON ACTivATEDSCARBON6HO
THE INFLUENCE OF TEMPERATURE AND TIME OF CARBON
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SIEOJ 64MCO
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE CONTRIBUTION OF CARBON FREE-RADICALS IN THE
S02 TO 503 OXIDATION PROCESS SIEOJ 65MCO
MECHANISM'OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THE CONCENTRATION OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND S02 OXIDATION
PROCESSES SIEDJ 66MCO
THE MECHANISM OF CATALYSIS AND A METHOD FOR THE SELECTION
~" FROM THE POINT OF VIEW OF INTERMEDIATE
PRODUCTS
TIKHAV40TMO
THE MECHANISMS OF OXIDATION HYDROGENATION AND
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BETWEEN DEPOLARIZING OXIDES ADSORBED ON CARBON AND
PLATINUM AND THE CATALYTIC ACTIVITY IN THE OXIDATION OF
SULFUR-DIOXIDE DAVTOK61TMO
CHEMISORPTION OESORPTION AND MECHANISMS OF CATALYTIC
REACTIONS ON METAL CATALYSTS KRAUA 63CDA
STRUCTURAL CHARACTERIZATION OF CATALYSTS
OF MERCURY
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PLATINUM FROM ALUMINOUS
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RECOVERY OF PRECIOUS METAL
CATALYSTS AND WASTES
NOBLE METAL RECOVERY PROCESS BERTRJ65NMR
SUPPORTED PLATINUM METAL CATALYSTS THEIR SELECTION AND
METHODS OF USE IN INDUSTRIAL PROCESSES
PLATINUM METAL ALLOYS IN ELECTROCATALVSIS A
EVALUATION OF RELATIVE ACTIVITIES
METAL SPRAYING TESTS IN LABORATORY AND ON
THE EFFECT OF ALKALI MF.TAL SULFATES ON THE
PROPERTIES OF VANADIUM
THE EFFECT OF METAL OXIDE
TIN CHROMIUM CATALYST
BONDGC6SSPM
FURTHER
BROOEW66PMA
SITES
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CATALYTIC
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ADMIXTURES ON THE ACTIVITY OF THE
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EFFECT OF ALKALI METAL SULFATES ON THE ACTIVITY OF
V205 FOR THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVITY ~
VANAOIUM-PENTOXIDE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE JIRUP 63EOT
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVITY OF
VANADIUM-PENTOXIDE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE JIRUP 6IVPC
93
10/27/69
METAL
METALLIC
METALS
PAGE
POSSIBLE APPLICATIONS OF RHENIUM METAL AND ITS ALLOYS
REACTIVATION OF USED PRECIOUS METAL CATALYSTS KLE*H 51PAO
CHEMISORPTION DESORPTION AND MECHANISMS OF CATALYTIC**" 65ROU
REACTIONS ON METAL CATALYSTS KRAUA 63CDA
REACTIONS OF OXIDE CATALYSTS WHOSE OXYGEN EXCHANGES WITH THE
SUBSTRATE OXYGEN AND DEFINITION OF ACTIVE METAL OXIDE
ALKALINE EARTH METAL COMBINATION WITH S02 OF FLUE-GAS
IN A FLUE DUST CLOUD KRUEM 67AEM
NOBLE METAL ALLOYS AS ANODE ELECTROCATALYSTS NIEDLW67NMA
THE SEPARATION OF SUSPENDED NOBLE METAL CATALYSTS
POWDERED METAL REACTION AGENTS PARTIALLY EMBEDOEOR?NSMETALS°
SU°PORTS • SAES 66PMR
DEPENDENCE OF CATALYTIC ACTIVITY OF METAL ON THEIR POSITION
IN PERIODIC TABLE SOKOAM6600C
CERAMIC CATALYST HAVING A FLAME SPRAYED COATING OF A
PLATINUM FAMILY METAL TEAGED64CCH
CATALYTIC OXIDATION OF SULFUR-DIOXIDE ON METAL SURFACES
KINETIC STUDIES OF THE OXIDATION OF SULFUR-DIDXI DE^N' G48CO°
VANADIUM CATALYSTS PROMOTED RY ALKALI METAL SALTS
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ADSORPTION AND ENERGETIC PROPERTIES OF METALLIC CATALYSTS
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SPECIFIC CATALYTIC ACTIVITY OF METALLIC PLATINUM
FINELY DIVIDED METALLIC CATALYSTS EsIoVS66FDM
CHEMICAL DEPOSITION OF CATALYTICALLY ACTIVE PLATINUM ON
GRAPHITE AND METALLIC POWDERS AND SURFACES RHODRN67COO
CORROSION BEHAVIOR OF SOME METALLIC MATERIALS IN LIQUID
SULFUR-DIOXIDE RIVOL 66CBS
RELATION BETWEEN REACTIVITY AND STRUCTURE OF METALLIC
SURFACES SANDJV64RBR
NEW METHOD FOR DETERMINING THE COMPOSITION OF THE ACTIVE
CENTER OF A METALLIC CATALYST STRFZV67NMD
CATALYSIS OF SULFUR-DIOXIDE TO SULFUR-TRIOXIDE BY METALS AND
PLATINUM-GOLD ALLOYS BOREGK53COS
CATALYSIS OF THE CONVERSION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDF BY METALS AND PLATINUM GOLD ALLOYS
THE SPECIFIC CATALYTIC ACTIVITY OF METALS SULFUR-ofoXIOE°T
OXIDATION ON PLATINUM CATALYSTS CHESVS56TSC
GASEOUS CATALYSIS BY METALS OF THE PLATINUM GROUP
CATALYTIC OXIDATION Of SULFUR-DIOXIDE PRESENT IN FLUE-GASFS*
BY IONIZED SOLUTIONS OF HEAVY MfTALS GRODMK33COO
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METALS
PAGE 66
RECOVERY OF NOBLE METALS EVAPORATED FROM AMMONIA-OXIDATION
CATALYSTS HOLZH 65RON
CATALYTIC ACTIVITY OF METALS LANDMA6f
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DEPOSITING METALS ON SILICEOUS CATALYST SUPPORTS FROM AMINE
... AOUEnus AMMONIA SOLUTIONS HULABF67P ~
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BETWEEN CATALYTIC ACTIVITY OF SOME METALS AND THEIR
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CATALYSIS OVER SUPPORTED METALS SINFJH67CSM
GENERAL RULE OF THE CATALYTIC ACTIVITY OF METALS
TANAK 66GRO
REACTIVATION OF PETROLEUM REFORMING CATALYSTS CONTAINING
PLATINUM METALS TOMAZ 66ROP
TYPES OF CORROSION AND BEHAVIOR OF METALS AND ADDITIVES IN
BOILER FURNACES HICKK 65TCB
A STUDY OF ADSORPTION ISOTHERMS ON OXIDE FORMS OF
METALSILICATE CARRIERS AND CATALYSTS
ZULFZG66SA1
SCRUBBING AND UTILIZATION OF EXHAUST GASES FROM METALURGICAL
FACTORIES IN THE NORTHERN USSR SHABAP63SUE
MULTIPLE AUTOMATED MICRO UNITS ACKEC067MAM
MICROANALYSIS
DETERMINATION OF TRACES AND THE MICROANALYSIS OF GASES
AND VAPORS HARM 66DTM
MICROCOULOMETRIC
IMPROVED SULFUR-REACTING MICROCOULOMETRIC CELL FOR
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SUL"FuR-OXIOE REACTIONS RADIOACTIVE SULFUR AND MICROPROBE
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ELECTROSTATIC DEPOSITION OF SULFURIC-ACID MISTS FROM THE
WASTE GASES OF SULFURIC-ACIO MANUFACTURE STOPK 65EOS
ACTIVITY STRUCTURE AND ELECTRICAL PROPERTIES OF MIXED
VANADIUM CATALYSTS EZHKZI64ASA
OPTIMUM PROCESS CONDITIONS FOR A COMPLETELY MIXED MULTISTAGE
REACTOR KUBOH 610PC
THEORY OF MIXED CATALYSTS RIENG 59TMC
SEM[CONDUCTANCE AND CATALYSIS RELATION BETWEEN
CATALYTIC ACTIVITY STO ICHIONE TRIC COMPOSITION AND STATE
OF ELECTRON LINKAGE FOR N-CONDUCTING MIXED CATALYSTS (IF
THE HOPCALITE-TYPE 'I II. RELATION BETWEEN CATALYTIC
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TYPE RIENG A4SAC
101
STUDIES OF CORROSION AND DEPOSITS KRAUHH68SOR I
MILLS-PACKARD-PROCESS ;
OPTIMUM COMPOSITION OF NITROSE IN SULFUR IC-ACI0 PRODUCTION
BY THE MILLS-PACKARO-PROCESS TSEIAN660CO
10/27/69
MIXED
MIXING
MIXTURE
MIXTURES
MN02
MNS04
MODEL
MODELLING
PAGE
67
EFFECT OF ADDITIVES ON OXIDE CATALYSTS
SEMICONDUCTIVITY
AND CATALYSIS QUANTUM ASPECTS OF CATALYSIS
ILLUSTRATED BY INVESTIGATIONS USING MIXED OXIDE CATALYSTS
INVERS MIXED CATALYSTS
IRON-OXIDE CATALYST ON A
ABSORPTION OF SUL FUR-DIOX IDI
JCHEJ 64EAO
iULFUR-TRIOXIOE SYNTHESIS USING
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! IN AN IDEALLY MIXED LAYER
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CATALYTIC MIXING MANUFACTURE AND UTILIZATION MI CHE 62CMM
GAS MIXING AND MOVEMENT OF SOLID PARTICLES IN A
FLUIDIZED-BED . TRABDG62GMA
PURIFYING A GAS MIXTURE FROM SULFUR-DIOXIDE AMELAG67PGM
ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE AQUEOUS
SOLUTION FROM A GAS MIXTURE BLASH 66ASO
OXIDATION OF S02 BY 02 OR 02-03 MIXTURE IN THE PRESENCE OF
SILICA-GEL ADSORPTION OF 02 ON SILICA-GEL ALUMINA-GEL AND
COTTON BRINE 4300S
ACTION OF THE REACTANT MIXTURE ON THE CATALYST IN THE COURSE
OF CATALYSIS ROZOAY64AOT
DESIGN OF CONTACT PROCESS EQUIPMENT WITH AN ADIABATIC
CATALYST LAYER FOR THE OXIDATION OF SULFUR-DIOXIDE DESIGN
Of EQUIPMENT WITH THE INTRODUCTION OF COLD REACTION
MIXTURES AND WITH INTERMEDIATE HEAT EXCHANGERS
BESKVS63DOC
REMOVING SULFUR-TRIOXIDE FROM GAS MIXTURES BURKOB68RST
ALLOWANCE FOR THE TEMPERATURE DEPENDENCE OF SPECIFIC HEAT
OF INDIVIDUAL GASES AND GAS MIXTURES IN THERMODVNAMIC
CALCULATION FOR GAS FLOW MACHINE FISCS 65ATD
THERMAL-CONDUCTIVITY OF BINARY MIXTURES OF SULFUR-DIPXinE
AND INERT GASES GUPTAD67TCB
COMPARATIVE RESULTS FOR THERMAL AND ELECTRONIC ACTIVATION OF
MIXTURES OF SULFUR-DIOXIDE AND OXYGEN MOYEAJ65CRF
REMOVAL OF S02 FROM GAS MIXTURES SHEL 65ROS
CONTINUOUS REMOVAL OF SULFUR-DIOXIDE FROM GAS MIXTURES
BY A FLUIDIZED LAYER OF SOLID GRANULAR ABSORBENT
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INFLUENCE OF THE ULTRASONIC FIELD DN THE CATALYTIC ACTIVITY
OF MN02 PREPARED BY ELECTROLYSIS KPWAE 6SIUF
THE REACTION OF SO? AND 02 IN AQUEOUS SOLUTIONS ON MNS04
COUGDP6STRn
THE HYDROOYNAMIC MODEL OF A FL III 01 ZED-BED ABAEGN64THM
MATHEMATICAL MODEL UF CATALYTIC REACTORS GENERAL PRINCIPLES
CYBUA 67MMC
A COMPUTATIONAL MODEL FOR THE STRUCTURE PF POROUS MATERIALS
EMPLOYED IN CATALYSIS FCSTRN66ACM
AERODYNAMIC MODELLING OF CONTACT APPARATUS MODELLING OF A
REACTOR FOR THE OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE ERMAA 68AMO
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10/27/69
MODELLING
MODELS
MULTIPLE
MULTIPLE-RED
MULTIPLET
MULT I UN IT
NH3
NICHROME
NICKEL
PAGE 68
MODELLING OF CHEMICAL REACTORS HEAT AND MASS TRANSFER WITHIN
""ULTS °F *
REACTION-RATE MODELLING IN HETEROGENEOUS CATALYSIS
K I TT I Rfk 7R R M
MODELLING OF CHEMICAL REACTORS VI. HEAT AND MASS TRANSFER
IN A POROUS CATALYST PARTICLE THE MULTIPLICITY OF SOLUTION
FOR THE CASE Of AN EXOTHERMIC ZERO-ORDER REACTION
MAREM 68HOC
MATHEMATICAL MODELS OF CATALYTIC REACTORS HEAT AND MASS
TRANSFER CYBUA 67MMO
FIXEO-rBED CATALYTIC REACTORS II. ONE DIMENSION STATIC MODELS
WITHOUT HEAD LOSSES KAZIC 67FBO
SOME PARAMETER ES.T.1MAT ION. CONSIDERATI ONS FOR HETEROGENEOUS
KINETIC MODELS MEZAR 66SPE
THE INTERPRETATION OF INITIAL RATE DATA WITH THE USE
OF
MEZAR 67TIO
PARRG 66SMI
HOUGEN-WATSON MODELS
SURFACE MODELS IN HETEROGENEOUS CATALYSIS
MULTIPLE AUTOMATED MICRO UNITS
INSTALLATIONS FOR INDUSTRIAL GAS CLEANING PROCESS
OPTIMIZATION FOR OPERATING MULTIPLE INSTALLATIONS IN ANY
ACKEC067MAM
REGIME
MULTIPLE-BED CATALYTIC REACTORS
NEW DATA ON THE MULTIPLET THEORY OF CATALYSIS
MULTIUNIT CATALYTIC ASSEMBLY
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METT 62MBC
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FROM CONTACT SULFURIC-ACID INSTALLATION CHEM 65UOS
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SULFIDE ON
COMPLEX SPIRALS OF PLATINIZED NICHROME KOTFNZ57COO
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SyLFinE
ON COMPLEX SPIRALS OF PLATINIZED NICHROME
KOTENZ57COS
THE CATALYTIC ACTIVITY OF PLATINIZED NICKEL IN THE OXIDATION
OF SULFUR-DIOXIDE DAVTOK61TCA
NICKEL SILICON ALLOYS HAYNFG67NSA
EFFECT OF HYDRPGEN-SULFIDE AND SULFUR-DIOXIDE ON THE
CORROSION OF CHEMICALLY RESISTANT CHROMIUM NICKEL STEEL
IN A SODIUM-SULFATE SOLUTION ACIDIFIED WITH SULFURIC-ACID
HERBG 66EHS
IN
EFFECT OF HIGH TEMPERATURE
SUBSEQUENT QUENCHING ON THE CORR
PLASTIC DEFORMATION AND
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PROPERTIES OF CHROMIUM NICKEL AUSTENTIC STF.ELS
SHVAGL63CMF
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10/27/69
NIOBIUM
NITRATES
NITROGEN
PAGE 69
ACTION OF SULFUR-DIOXIDE ON TITANIUM ZIRCONIUM HAFNIUM
VANADIUM NIOBIUM AND TANTALUM DAVIL 62ASD
DECOMPOSITION PRESSURES OF NITRATES ANO SULFATES
MEASUREMENTS OF SODIUM-VANADATES
NEUMB 35DPO
NITROGEN-OXIDE
NITROGEN-OXIDES
NITROSE
ELECTRIC DISCHARGE APPARATUS FOR THE SYNTHESIS OF
NITRIC-OXIDE FROM ATMOSPHERIC NITROGEN COTTWJ49EDA
REACTION OF SULFUR-DIOXIDE WITH ACTIVE NITROGEN
JACOA 66RSD
SIMULTANEOUS RECOVERY OF SULFUR-DIOXIDE AND THE PRODUCTION
OF NITROGEN FERTILIZERS VASINA60SRS
REMOVAL OF NITROGEN-OXIDE CONTAINING SULFUR IC-AC ID FUMES
LAMMC 66RNO
EFFECT OF SULFUR IC-ACID CONCENTRATION ON REGENERATION OF
NITROGEN-OXIDES IN A TOWER SYSTEM SAVIEI66EOS
PURIFICATION OF NITROSE EXHAUST GASES GANZSNA&PNE
_y FORMATION IN THE PRESENCE OF SALTS IN
THE VELOCITY OF ACID
OXIDATION OF SULFUR-DIOXIDE BY NITROSF
GLADVI63TVO
IN SULFURIC-ACID
KUNITI4600S
PREPARING SULFURIC-ACIO BY THE NITROSE METHOD
MIKHK 67PSA
PREPARATION OF SULFURIC-ACID BY NITROSE METHOD
MORDBI67POS
OXIDATION OF SULFUR-DIOXIDE WITH NITROSE A SOLUTION OF
NITROSYLSULFURIC ACID IN SULFUR 1C ACID IN PACKED COLUMNS
- IN SIEVE PLATE COLUMNS PETEA_6300S
AND IN SIEVE PLATE COLUMNS
PTIMUM COMPOSITION OF NITRC,
BY THE MILLS-PACKARD-PROCE!
OPTfiMyMjCOMPOSITION OF NITROSE IN SULFURIC-ACID PRODUCTION
OXIDATION OF SULFUR-DIOXIDE WITH NITROSE
NITROSYLSULFURIC ACID IN SULFURIC ACID
AND IN SIEVE PLATE COLUMNS
PETE
ROOIU
TSEIAN660CO
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NOMOGRAMS
OXIDATION OF S02 IN AIR AT 95C-DEGREES
INFLUENCE OF CO AND NO
NOBLE METAL RECOVERY PROCESS BERTRJ6
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IN PACKED COLUMNS
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RECOVERY OF NOBLE METALS E .-. -
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NOBLE METAL ALLOYS AS ANODE ELECTROCATALVSTS NIEOLW67NMA
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CONVE
OLEUM
CONVERTED"INTO"SULFUR-TRIOXIDE ANCi THE COMPOSITION OF
SHRASS36NCP
NON-HYDROCARBONS
THERMO PROPERTIES OF NON-HYDROCARBONS
PROPERTIES DF SULFUR-DIOXIDE
THERHODYAMIC
CANJLN66TPN
1GI,
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10/27/69
NON-UNIFORM
NOZ
NUCLEAR
OLEUM
OPTIMAL
OPTIMIZATION
CATALYTIC PROCESSES ON NON-UNIFORM SURFACES
PHOTOLYSIS OF NOZ IN THE PRESENCE OF S02
PAGE 70
TEMKHl*9CPO
AT 3660-4
JAFFS 66PON
PROSPECTS FOR NUCLEAR RADIATION APPLICATION IN CATALYSIS
CIBOS 65PFN
PROSPECTS FOR NUCLEAR RADIATION APPLICATION IN CATALYSIS
CIBOS 67CNR
EFFECT OF NUCLEAR RADIATION ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE REACTION OF S02 OXIDATION KOZAZ 66EON
EQUILIBRIUM PRESSURE OF SULFUR-TRIOXIDE VAPORS OVER OLEUM
THE ABSORPTION OF SULFUR-TRIOXIDE IN BUBBLE CAP PLATE
ABSORBERS FOR THE PRODUCTION OF OLEUM AKSEYV64TAO
PREPARATION OF OLEUM AMELAG66POO
MANUFACTURING UP TO 60 PER CENT OLEUM OR SULFURIC-ACID
OERKJ 64TUT
PRODUCTION OF OLEUM IN THE MANUFACTURE OF SULFURIC-ACID BY
THE SHORTENED CONTACT PROCESS REZIIG6SPOM
NOMOGRAMS FOR CALCULATING THE PERCENTAGE OF SULFUR-DIOXIDE
CONVERTED INTO SULFUR-TRIOXIDE AND THE COMPOSITION OF
OLEUM SHRASS36NCP
CONTROL OF TEMPERATURE BY ADMISSION OF A COLD COMPONENT AS A
MEANS FOR ENSURING OPTIMAL CONDITIONS FOR AN EXOTHERMIC
REACTION FEOOAV67COT
CALCULATION OF THE OPTIMAL CONDITIONS FOR CHEMICAL REACTORS
OF THE COMBINED TYPE KINGRP65COT
OPTIMAL AOIABATIC BED REACTORS FOR SULFUR-DIOXIDE WITH COLD
SHOT COOLING LEE KY630AB
OPTIMIZATION OF THE PROCESS OF SULFUR 1C-AC-ID PRODUCTION BY
THE CONTACT METHOD AMELAG660OR
OPTIMIZATION OF CATALYTIC PROCESSES IN INDUSTRIAL REACTORS
SIMULATION AND OPTIMIZATION OF CHEMICAL REACTORS B°R GK6
SOME TOPICS IN OPTIMIZATION OF REACTORS WITH CATALYST
OEACTIVATION CHOUA 67STO
THE OPTIMIZATION OF BI FUNCTIONAL CATALYST SYSTEMS
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REACTIONS DYS0006TROP
INSTALLATIONS FOR INDUSTRIAL GAS CLEANING PROCESS
OPTIMIZATION FOR OPERATING MULTIPLE INSTALLATIONS IN ANY
REGIME FERRG 66IFI
STANDARD PROGRAMS FDR THE OPTIMIZATION OF PROBLEMS IN
CHEMICAL TECHNOLOGY HOFMH &«SPF
OPTIMIZATION OF AN ADIABATIC STAGE REACTOR LANGD 6400A
AUTOMATIC OPTIMIZATION OF THE OXIDATION OF SULFUR-DIOXIDE
LIBELMfc«AOn
10/27/69
OXYGEN
OZONE
PAGE 72
ISOTOPE EXCHANGE FOR THE OXYGEN OF VANAOIUM-PENTOXtOE WITH
SULFUR-DIOXIDE AND TRIOXIDE KASALA64IEF
INFLUENCE OF TEMPERATURE ON THE OXIDATION OF SULFUR-DIOXIDE
WITH OXYGEN IN THE PRESENCE OF CATALYSTS AND CATALYST
POISONS KASHLI35IOT
FORMATION OF INTERMEDIATE COMPOUNDS IN THE OXIDATION OF
SULFUR-DIOXIDE WITH OXYGEN KASHLI36FOI
OXIDATION OF SULFUR-DIOXIDE BY OZONE IN THE PRESENCE OF
MTRATIONS KASHLI3
OXYGEN IN VARIOUS CONCENTRATIONS
KASHLI3800S
THE OXIDATION OF GASES HIGH IN SULFUR-DIOXIDE AND OXYGEN IN
THE PRESENCE OF A VANADIUM CATALYST MRRIP3ATOO
THE POSSIBILITY OF ELECTROCHEMICAL OXIDATION OF
SULFUR-DIOXIDE BY ELECTROLYTIC OXYGEN KLYAGL62TPO
REACTIONS OF OXIDE CATALYSTS WHOSE OXYGEN EXCHANGES WITH THE
SUBSTRATE OXYGEN AND DEFINITION OF ACTIVE METAL OXIDE
KRAUA 67ROO
OXIDATION OF AMMONIACAL SULFUR-DIOXIDE SOLUTION WITH
OXYGEN IN A STIRRED AUTOCLAVE MAHABK64OAS
COMPARATIVE RESULTS FOR THERMAL AND ELECTRONIC ACTIVATION OF
MIXTURES OF SULFUR -DIOXIDE AND OXYGEN MOYEAJ65CRF
A CHEMICAL PROCESS FOR THE PRODUCTION OF OXYGEN
MUKHIPS7ACP
THE KINETICS OF REACTION BETWEEN OXYGEN ATOMS AND
S02 AN INVESTIGATION BY ELECTRON-SPI N-RESQNANCE
SPECTROMETRY MULCMF67KRO
CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH HEAVY OXYGEN
41COS
THE OXIDATION OF GASES HIGH IN SULFUR-DIOXIDE AND OXYGF.N IN
THE PRESENCE OF A VANADIUM CATALYST POSTVF3*TOO
A NEW METHOD OF EXAMINING THE REACTIONS OF OXYGEN ATOMS
REUBBG60ANM
THE ROLE OF THE OXYGEN OF VANAOI UM-PENTOXIDE CATALYSTS IN
THE CATALYSIS OF OXIDATION ROITVA58TRO
REMOVAL OF SULFUR-DIOXIDE FROM OXYGEN CONTAINING GASES
SHEL 66ROS
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SURFACE BY THE ELECTROCHEMICAL METHOD IN OXYGEN
CHEMISORPTION SIEDJ 6SDNA
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CARBON-MONOXIDE SULFUR-DIOXIDE OXYGEN SYSTEM
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HEAVY HYDROGEN AND OXYGEN
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A STUDY BY THE OPTICAL METHOD OF THE BEHAVIOR OF THE
CATALYST IN STRONGLY ACID SOLUTIONS IN
MANGANESE SALT _
THE PRESENCE OF OZONE
KASHLI3SASB
OXIDATION OF SULFUR-DIOXIDE BY OZONE IN THE PRESENCE OF
OXYGEN IN VARIOUS CONCENTRATIONS '
KASHLI3ROOS
105-
107
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10/27/69
OPTIMIZATION
OPTIMIZED
OPTIMUM
ORDER
ORE
OXIOATIVE
OXVGEN
PAGE
71
THE APPLICATION OF A GRADIENT METHOD TO THE OPTIMIZATION OF
ADIABATIC MULTISTAGE CATALYTIC REACTORS LUOUF 67TA01
THE OEACTIVATION OF CATALYSTS AND SOME RELATED OPTIMIZATION '
PROBLEMS SZEPS 67DCS |
SULFURIC-ACID OPTIMIZED CONDITION IN CONTACT MANUFACTURE <
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SULFURIC-ACID PRODUCTION BOREGK37TOC'
OPTIMUM CONTROL OF SULFURIC-ACID PRODUCTION WITH THE AID
OF COMPUTERS GAFUAA650CO ;
FIND OPTIMUM CATALYST REGENERATION CYCLE HART 67FOC
OPTIMUM CONDITIONS FOR CAS-SOLID CATALYTIC REACTION PROCESS
IN A FIXED-BED . • KUBOH 590CF
OPTIMUM PROCESS CONDITIONS FOR A COMPLETELY MIXED MULTISTAGE
REACTOR KUBOH 610PC
OPTIMUM SHAPES AND SIZES OF ELEMENTS OF A VANADIUM CATALYST
FOR THE PRODUCTION OF CONTACT H2S04 MALKVI640SA
OPTIMUM CONDITIONS OF MAGNESITE REMOVAL OF SULFUR-DIOXIDE
FROM EXHAUST-GASES PINAVA630CM{
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OPTIMUM SHAPE AND SIZE OF CATALYST GRAINS SLINMG640SS*
OPTIMUM SHAPE AND GRAIN SIZE FOR A VANADIUM CATALYST
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BY THE MILLS-PACKARD-PROCESS TSEIAN660CO
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SULFURIC-ACID PRODUCTION FROM ORE ROASTER GASES nn|1|OJR67s,p
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SULFUR-TRIOXIOE PRODUCTION WITH OXYGFN BY THE CONTACT METHOD
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PAGE
73
ACTIVE FORM OF MANGANESE CATALYST IN THE OZONE CATALYTIC
METHOD OF OXIDATION OF SULFUR-DIOXIDE IN ACID SOLUTIONS
NEMKOG67AFO
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS VII EFFECT
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SULFURIC-ACIO PRODUCTION WITHOUT COLUMN PACKING
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OXIDATION OF SULFUR-1IQXIDE IN THE RANGE OF ATOMIC AND
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MODELLING OF CHEMICAL REACTORS HFAT AND MASS TRANSFER WITHIN
A POROUS CATALYST PARTICLE SOME RESULTS OF AN ANALYSIS
FOR A ZERO-ORDER REACTION HLAVV 67MOC
MODELLING OF CHEMICAL REACTORS VI. HEAT AND MASS TRANSFER
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10/27/69
PARTICLES
PARTI OJLATE
PD
PETROLEUM
PHENOL
PHOSPHATE
PHOSPHATIC
PAGF 74
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UNIFORM-SURFACE CATALYST IN A FLUIDIZED BED INVOLVING
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FORMATION OF SULFUR-TRIOXIDE UNDER THE ACTION OF ALPHA
PARTICLES MAISJE27FOS
EFFECT OF CONCENTRATION GRADIENTS OF REAGENTS AND THE
TEMPERATURE ON THE EFFICIENCY OF POROUS CATALYST PARTICLES
AND THE LIMITS OF EXISTENCE OF STEADY STATE CONDITIONS
PISMLM66EOC
EFFECTS OF THE DISTRIBUTION OF PORE LENGTHS IN CATALYST
PARTICLES ON THE CATALYST EFFICIENCY IN AN IRREVERSIBLE
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THE KINETICS OF OXIDATION OF GASEOUS SULFUR-DIOXIDE IN
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PHENOL KASHLI35TKO
COMPOSITE FERTILIZER FROM PHOSPHATE NITRIC-ACID AMMONIA AND
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FERTILIZER PLANT
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CONCENTRATION OF SULFUR 1C OR PHOSPHORIC-ACID
MARTTCftfcCSP
J.C9
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PHOSPHOR 1C-AC I OS
CORROSION BEHAVIOR OF CHROMIUM-NICKEL-MOLYBDENUM-COPPER
STEELS IN SULFURIC AND EXTRACTION PHOSPHORIC-ACIDS
SIDOYS67CBC
PHOSPHORUS
STABILIZING LIQUID SULFUR-TRIOXIDE WITH PHOSPHORUS
CONTAINING COMPOUNDS GILBEE64SLT
PHOTOCHEMICAL
nxIDATIQN OF_SyLFyP-DIOXIOE BY PHOTOCHEMICAL REACTION.ANO_
CK
PHOTOSENSITIZATION CHENSW5800S
DETECTION OF PHOTOCHEMICAL OXIDATION OF SULFUR-DIOXIDE
OUNHSB60DOP
PHOTOCHEMICAL OXIDATION OF SULFUR-DIOXIDE IN AIR
GERHER55POO
PHOTOLYSIS
PHOTOLYSIS OF N02 IN THE PRESENCE OF S02 AT 3660-A
JAFFS 66PON
PHOTOSENSITIZATION
OXIDATION OF SULFUR-DIOXIDE BY PHOTOCHEMICAL REACTION AND
PHOTOSENSITIZATIDN CHENSH5800S
PHTHAL1C-ANHYDRIDE
RECOVERY OF VANADIUM FROM THE SPENT V-K SILICA GEL CATALYST
USED IN PHTHALIC-ANHYDRIDE MANUFACTURING SHESAP65ROV
PILOT
PLATE
PLATES
PLATINIZED
PLATINUM
LUTION ANON 66NPP
SULFUR-DIOXIDE FROM HOT
NEW PILOT PLANTS TACKLE S02 POLLI
PROCESS DEVELOPMENT IN REMOVING i
FLUE GASES PILOT PLANT STUDY OF THE ALKALIZED
ALUMINA SYSTEM FOR SULFUR-DIOXIDE REMOVAL BIEND 67PDR
SULFURTOIOXIOE REMOVAL FROM INDUSTRIAL WASTE-GASES IN PILOT
AND FULL SCALE PLANTS HE ING 65SDR
FUR-DI
HE ALK
RE MOV
THE ABSORPTION OF SULFUR-TRIOXIDE IN BUBBLE CAP
ABSORBERS FOR THE PRODUCTION OF OLEUM
OXIDATION OF SULFUR-DIOXIDE WITH NI TROSE
NITROSYLSULFURIC ACID IN SULFURIC ACID
AND IN SIEVE PLATE COLUMNS
PLATE
AKSEYV64TAO
A SOLUTION OF
IN PACKED COLUMNS
PETEA 6300S
«!ASS TRANSFER IN A SCRUBBER
WITH CONE-SHAPED GRID PLATES
KHOKSF65MTS
THE CATALYTIC ACTIVITY OF
OF SULFUR-DIOXIDE
PLATINIZED SILICA-GELS AS CATALYSTS FOR
OF SULFUR DIOXIDE
PLATINIZED NICKEL IN THE OXIDATION
DAVTOK61TCA
THE OXIDATION
HOLMHN29PSG
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SULFIDE ON
COMPLEX SPIRALS OF PLATINIZED NICHROME KOTFNZ57COO
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SULFI HE
ON COMPLEX.SPIRALS OF PLATINIZED NICHROME
UTILIZING WASTE FROM THE ALUMINUM-CHLORIDE INDUSTRY FOR
CARRIERS OF PLATINUM IN THE OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE ADADIE34UHF
THE USE OF FE304 BY-PRODUCTS FROM BETA-NAPTHYLAMINE AS A
' PLATINUM CARRIER IN THE CONTACT OXIDATION OF S02
110
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PLATINUM
PAGE 76
RECOVERY OF PLATINUM FROM SPENT ALUMINUM-PLATINUM CATALYSTS
SUPPORTED PLATINUM METAL CATALYSTS THEIR SELECTION AND66"
METHODS OF USE IN INDUSTRIAL PROCESSES BONOGC65SPM
CATALYSIS OF THE CONVERSION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE BY METALS AND PLATINUM GOLD ALLOYS
BOREGK53COT
PLATINUM METAL ALLOYS IN ELECTROCATALYSIS A FURTHER
EVALUATION OF RELATIVE ACTIVITIES BROOEW66PMA
PRODUCTION OF A PLATINUM CATALYST BUKHSV65POA
SPECIFIC CATALYTIC ACTIVITY OF METALLIC PLATINUM
THE SPECIFIC CATALYTIC ACTIVITY OF METALS SULFUR-DIOXIDE
OXIDATION ON PLATINUM CATALYSTS CHESVS56TSC
RECRYSTALLIZATION OF SUPPORTED PLATINUM CONNJF67RSP
THE MECHANISMS OF OXIDATION HYOROGENATION AND
ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS RELATION
BETWEEN DEPOLARIZING OXIDES ADSORBED ON CARBON AND
' AND THE CATALYTIC ACTIVITY IN THE OXIDATION OF
DAVTOK61TMO
OF SUPPORTED PLATINUM DOUGNA65CAO.
GASEOUS CATALYSIS BY METALS OF THE PLATINUM GROUP
DUPAL 25GCB:
INFLUENCE OF CARBON-MONOXIDE ON THE ACTIVITY OF PLATINUM
CATALYSTS DURING THE OXIDATION OF SULFUR-DIOXIDE TO
ERENVY38IOC'
QUANTITIES OF ADDED PLATINUM ON THE >
_ _.. F VANADIUM-PENTOXIDE REGARDING THE
DXI DAT I ON OF HYDROGEN ILCHNI67TIO
MECHANISM FOR RECOVERY OF PLATINUM LOSSES DURING AMMONIA
CATALYTIC OXIDATION JANIW 67MFR
RECOVERY OF PLATINUM FROM CONSUMED PLATINUM CATALYSTS
KURPC 64ROP
REMOVING IRON FROM DEACTIVATED OIL TREATMENT CATALYSTS
CONTAINING PLATINUM LEOPJG65RIF
DELETERIOUS ACTION OF RHODIUM AND OF IRIDIUM UPON PLATINUM
_ SULFURIC-ANHYDRIDE LEVIG
PLATINUM .
SULFUR-DIOXIDE
CATALYTIC ACTIVITY
FUR-TRIOXIDE
.NFLUENCE OF SMALL _
ATALYTIC ACTIVITY OF
THE INFLUENi
HE CATALYS
LCVIGR27DAO
INFLUENCE OF ARSENIC DN THE CATALYTIC ACTIVITY OF PLATINUM
OF SULFUR-DIOXIDE
FOR THE OXIDATION OF SULFUR-DIOXIDE MAXTEB28IOA
THE STRUCTURE OF SUPPORTED PLATINUM CATALYSTS EXAMINATION
BY ELECTRON MICROSCOPY MOSSRL67SSP
CATALYTIC OXIDATION OF SULFUR-DIOXIDE BY HEAVY HYDROGEN
ON THE SURFACE OF A PLATINUM SPONGE NAKAS MCOH,
MECHANISM OF OXIDATION HVDROGENATION AND ELECTROCHEMICAL
COMBUSTION ON SOLID CATALYSTS LOW TEMPERATURE
OXIDATION ON PLATINUM
REJUVENATION OF PLATINUM CATALYST
CHEMICAL DEPOSITION OF CATALYTICALLY ACTIVE PLATINUM ON
GRAPHITE AND METALLIC POWDERS AND SURFACES RHODRN67CDO
REGENERATING PLATINUM CATALYSTS RIDLES29RPC.
- - 5TS SUCH fts THOSE USFD FOR
ERA
II. *mr
IKE
PLATINUM CATALYS
TH
iXiOATlON OF SULFUR-OinxIDE R1DLES29RPO
KINETICS OF OXIDATinN OF SULFyRrDIOXIDE ON A PLATINUM
CATALYST UNDER
SULFUR-DIOXIDE
EQUILIBRIUM CONDITIONS
ROITVA60TKO
10/27/69
PLATINUM
PLATINUM-GOLD
PAGE 77
REGENERATION OF A PLATINUM CATALYST BY OXIDATION AND
r.I5.EAIMlNJ«Mi!H,A HXDR°GEN-CONTAINING GAS SCHWEF66ROA
CATALYTIC OXIDATION OF SULFUR-DIOXIDE KINETICS OF
OXIDATION I OF SULFUR-DIOXIDE IN THE RANGE OF ATOMIC AND
CRYSTALINE LAYERS OF PLATINUM AND PALLADIUM
REGENERATION AND REACTIVATION OF .DEACTI VATED PLATINUM
CATALYST ON A CARRIER SHEL 62RAR
REGENERATION AND REACTIVATION OF A PLATINUM REFORMING
CATALYST SHEL 67RAR
MECHANISM OF ELECTRQOX IDAT ION OF SOME COMPOUNDS ON PLATINUM
SHLYAI56MOE
DIFFERENCE IN THE OXIDATION PROCESSES OF SULFUR-DIOXIDE
AND HYDROGEN ON A PLATINUM CATALYST UNDER THE CONDITIONS
OF CHILLING AND THE APPLICATION OF AN ELECTRIC FIELD
STADPM65DIT
OXIDATION OF SULFUR-OIOX IDE OVER A PLATINUM CATALYST UNDER
THE CONDITIONS OF ANNEALING AND THE APPLICATION OF AN
ELECTRIC CHARGE TO THE CATALYST STETKG620OS
CERAMIC CATALYST HAVING A FLAME SPRAYED COATING OF A
PLATINUM FAMILY METAL TEAGED64CCH
REpflLCAT,NUM°ME?ALs'ETR°LEUH «F°R>"™ CATALYSTS CONTAINI NG
STUDY OF THE OXIDATION OF SULF UROUS-ANHYOR IDE AND AMMONIA
GAS IN THE PRESENCE OF PLATINUM AND RHODIUM
C*PL AT I
1- ALLOYS
SULFUR-TR ' OXIDE
WENGP I8SOT
BY METALS AND
BOREGK53COS
ANODIC OXIDATION OF SULFUR-DIOXIDE ON GOLD AND PLATINUM-GOLD
ALLOYS LEZHKA61AOO
PLATINUM-PALLADIUM
PLATINUM-SUPPORTED
ADSORPTION STUDIES OF PLATINUM-SUPPORTED CATALYSTS
POISONED BUTYPY52ASO
POISONING
"SENIC •» ggHER
CATALYST POISONING AND GEOMETRY OF THE CATALYST PARTICLE
CAGIS 67CPG
TIME-DEPENDANT PORE-MOUTH POISONING OF CATALYSTS
CARBJJ66TOP
PHENOL
KASHLI35TKO
111
112
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POISONING
POISONS
POLYESTER
POLYMER
PORE
PORE-MOUTH
PORES
POROSITY
POROUS
PAGE
78
POISONING OF VANADIUM CATALYSTS USED IN THE OXIDATION OF
SULFUR-DIOXIDE IN A FLUIDI ZED-BED MUKHIP65POV
EFFECT OF CATALYST POISONING ON THE OVERALL SELECTIVITY AND
ACTIVITY SADAE 67EOC
THE POISONING OF CHROMIUM CATALYSTS BY ARSENIC AND OTHER
CONTACT POISONS ADAOIE35TPO
EFFECTS OF POISONS ON POROUS CATALYST ACTIVITY
EFFECT OF POISONS ON POROUS CATALYST ACTIVITY
GIOLF 67ERP
GIOLF 67EPP
INFLUENCE OF TEMPERATURE ON THE OXIDATION OF SULFUR-DIOXIDE
WITH OXYGEN IN THE PRESENCE OF CATALYSTS AND CATALYST
POISONS KASHLI35IOT
.ECONOMIC ELIMINATION OF AIR POLLUTION THROUGH RECOVERY
PRODUCTS IN POLYESTER GAS SCRURBERS HAMPNH65EEA
POLYMER ABSORBENT FOR
OXIDATION
SULFUR-DIOXIDE THAT PROMOTES ITS
YANEJF65PAS
HEAT TRANSFER ANALOGY FOR DIFFUSION AND FIRST ORDER CHEMICAL
REACTION IN A CATALYST PORE COUGRH67HTA
EFFECT OF PORE GEOMETRY ON THE ACTIVITY AND AGING OF
CATALYSTS FERRG 67EPG
PORE DISTRIBUTION IN POROUS CATALYSTS GRUNE 66POI
PORE STRUCTURE AND GASEOUS DIFFUSION IN SOLID CATALYSTS
JOHNMF65PSA
PORE STRUCTURE AND GASEOUS DIFFUSION IN SOLID CATALYSTS
JOHNMF65PSG
EFFECTS OF THE DISTRIBUTION OF PORE LENGTHS IN CATALYST
PARTICLES ON THE CATALYST EFFICIENCY IN AN IRREVERSIBLE
-- — TARTR 66EDP
SURFACE REACTION OF THE FIRST ORDER
PORE STRUCTURE IN CATALYSTS
SELECTIVITY FOR SUCCESSIVE FIRST ORDER REACTION AND CATA.
PORE STRUCTURE DURING HIGH DIFFUSIVE RESISTANCE PROCESSES
TARTR 67SSF
TARTR 66PSC
LYST
TIME-DEPENDANT PORE-MOUTH POISONING OF CATALYSTS
CARBJJ66TOP !
EFFECT OF IRREGULAR PORES ON THE SELECTIVITY OF A POROUS
CATALYSTS FERRG 67EIP
CALCULATION OF THE RATE OF A HALF ORDER REACTION PROCEEDING
IN PORES OF A CATALYST GLASV 66COT
POROSITY OF ABSORBENTS AND CATALYSTS
REGULATION OF POROSITY AND MECHANICAL STRENGTH OF SHAPED
DUBIMM66PAC
KIESELGUHR CATALYST CARRIERS
JELIJF65RPM
INVESTIGATIONS OF POROUS ADSORBENTS AND CATALYSTS BY MEANS
OF DISTRIBUTIVE FUNCTIONS OF THE SURFACE WITH REGARD TO
ITS CURVATURE BUKUI 661 PA
10/27/69
MQROUS
PAGE 79
EFFECT OF A POROUS SILICA-GEL CATALYST CARRIER ON THE
VELOCITY OF OXIDATION DF SULFUR-DIOXIDE GAS
8HUFGI34EOA
UBIMM66PSA
EFFECT OF IRREGULAR PORES ON THE SELECTIVITY OF
CATALYSTS
POROUS CERAMIC BALLS FOR CARRYING CATALYSTS
A COMPUTATIONAL MODEL ~ ~
POROUS STRUCTURE OF AOSORB&NTS AND CATALYSTS
IMPROVEMENT OF THE MASS TRANSFER FROM A GAS TO A POROUS
CATALYST OR ADSORBENT BY PRESSURE OSCILLATIONS
ESSO 64IMT
A POROUS
FERRG 67EIP
_ _ .... FISCHC64PCB
._. _ FOR THE STRUCTURE OF POROUS MATERIALS
EMPLOYED IN CATALYSIS FOSTRN66ACM
EFFECTS OF POISONS ON POROUS CATALYST ACTIVITY
GIOLF 67EOP
EFFECT OF POISONS ON POROUS CATALYST ACTIVITY
GIOLF 67EPP
MODELLING OF CHEMICAL REACTORS HEAT AND MASS TRANSFER WITHIN
A POROUS CATALYST PARTICLE SOME RESULTS OF AN ANALYSIS
FOR A ZERO-ORDER REACTION HLAVV 67MOC
POROUS ACTIVATED ALUMINA OF HIGH MECHANICAL STRENGTH
HUTTJC65PAA
ELECTRON-MICROSCOPIC STUDY OF THE POROUS STRUCTURE OF A
VANADIUM CATALYST FOR S02 OXIDATION KARADB65EMS
THE INFLUENCE OF EXTERNAL DIFFUSION INHIBITION ON THE
PROCESS IN A POROUS CATALYST LEVIVG66TIO
MODELLING OF CHEMICAL REACTORS VI. HEAT AND MASS TRANSFER
IN A POROUS CATALYST PARTICLE THE MULTIPLICITY OF SOLUTION
FOR THE CASE OF AN EXOTHERMIC ZERO-ORDER REACTION
MAREM 68MOC
EFFECT OF CONCENTRATION GRADIENTS OF REAGENTS AND THE
TEMPERATURE ON THE EFFICIENCY OF POROUS CATALYST Pt
AND THE LIMITS OF EXISTENCE OF STEADY STATE CONDITIONS
PISMLM66EOC
INCREASING THE MECHANICAL STRENGTH OF POROUS DISPERSE BODIES
ADSORBENTS AND CATALYSTS REBIPA6MMS
EFFECTIVENESS FACTOR FOR POROUS CATALYSTS LANGNUIR-HINSHEL
WORD KINETIC EXPRESSIONS ROBEGW65EFF
EFFECTIVENESS FACTORS FOR POROUS CATALYSTS RPBEGW65EFP
SOME PROBLEMS IN THE PHVSIOCHEMICAL THEORY OF THE
STABILITY OF FINELY DISPERSED POROUS BODIES CATALYSTS AND
SORRENTS SCHCED6SSPP
POROUS SUPPORT FOR FLUIDIZED-BED CATALYSTS SELIHJ67PSF
MAXIMUM TEMPERATURE INSIDE A PORDUS CATALYST WEI J 66MTI
POROUS-BED
POROUS-BED DIFFUSION USING VHt FREQUENCY RESPONSE METHOD
BILLJ 67PBD
POTASH-MAGNESITE
CYCLIC POTASH-MAGNESITE METHOD FOR REMOVING
SULFUR-DIOXIDE FROM GASES i>TNAVA67CPM
POTASSIllM-OXIDE
EFFECT OF POTASSIUM-OXIDE ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE OXIDATION — -- --
TEMPERATURES
CLES
OF SULFUR-DIOXIDE AT~LOW
GFRPEW.1FPP
113
13*1
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pnuER
PRECIPITATION
PRECIPITATOR
PRECIPITATORS
PREDICTION
PREHEATING
PAGE
POTASSIUH-VANADIUM-DXIOE CATALYSTS
Qf SULFUR.DIOXlo£
MARSP 64TMC
EVALUATION OF DRY PROCESSES FOR REMOVING S02 FROM POWER
PLANT FLUE GASES BIEND 65EOP
AIR POLLUTION FROM POWER STATIONS CRAXSR66APF
SULFUR-DIOXIDE REMOVAL AND RECOVERY FROM PULP MILL POWER
PLANTS GALESF67SDR
CONTROL OF AIR POLLUTION FROM LARGE THERMAL POWER STATIONS
. GARTFE66COA
AIR POLLUTION CONTROL MEASURES TAKEN AT THE POWER STATION
IN YOKKAICHI DISTRICT MIYAM 66APC
POWER INDUSTRY-CHIMNEYS PIERRR66PIC
SULFUR-DIOXIDE AND FLY ASH REMOVAL FROM COAL BURNING
POWER 'PLANT POLLWA67SDF
REMOVAL OF SULFUR-DIOXIDE FROM POWER PLANT STACK GASES
REESRL RSD
PRECIPITATION OF SULFUR-DIOXIDE FROM HOT FLUE GASFS
KIYOR 66PC1S
INCREASED PRECIPITATION RATE OF ELECTROSTATIC SEPARATORS
ORNEN 66EP
ELECTROSTATIC PRF.CIP ITATOR
CONDITIONING OF STACK GASES FOR ELECTROSTATIC PRECIPITATORS
HARLEV56COS
ANALYTICAL PREDICTION OF CONCENTRATION AND TEMPERATURE
PROFILES IN A PACKED CATALYTIC TUBE TONES 66APO
PREHEATING A CATALYTIC REACTOR BY DIRECT FEED OF FUEL GASES
TO THE CATALYST MATERIAL OSMUVA64PAC
PREPARATION OF OLEUM AMELAG66POO!
THEORETICAL SELECTION PREPARATION AND USE OF INDUSTRIAL i
CATALYSTS 80REGK64TSR
PREPARATION OF SULFURIC-ACID WITHOUT A CATALYST AT HIGH '
PRESSURE BURYKA64PSA
PREPARATION OF SULFURIC-AC10 CHEM 66POS
A STUDY ON INDUSTRIAL PREPARATION OF AMMONIUM-SULFATE
BY NONCATALYTIC OXIDATION CHUNKY66SIP
PREPARATION OF VANADIUM-BASE CATALYSTS FOR THE SULFUPIC-AC ID
INDUSTRY DIACV 55POV
THE PREPARATION OF WEAR RESISTANT IRON-OXIDE CATALYST
DOBKEI66TPO
ETF UXIDATION WITHOUT FLAME AND THEIR
CA?SCYCSET"F85 SESaSMIffilD PREPARATION
A SIMPLIFIED PREPARATION FOR SULFURIC-ACID
PREPARATION OF SULFUR IC-AC 10 BY NI TRDSE MF. THOO
GENE 67CFC
HAMPG 64CSA
MONT 65ASP
unnftn i L •» n nf
A NEW METHOD FOR THE PREPARATION OF CONTACT CATALYSTS
RIOGD
10/27/61
PREPARATION
PREPARING
PRESSURE
PRESSURES
PRINCIPLES
PROCESS
PAGE
81
PREPARATION OF CATALYSTS USING A FLUX
PREPARATION OF CORUNDUM CARRIERS FDR CATALYSTS
UNIT 64POC
ZLATSG66PCC
SCIENTIFIC BASES FOR SELF.CTING AND PREPARING CATALYSTS
RATIONAL BASIS FOR PREPARING CATALYSTS
PREPARING CORUNDUM CARRIERS FOR CATALYSTS GRIGAF68PCC
PREPARING SULFUR1C-ACIO BY THE NITROSE METHOD
MIKHK 67PSA
REASONS FOR THE RISE IN THE TEMPERATURE OF GASES IN FRONT
OF THE CONTACT APPARATUS OF AN INSTALLATION FOR PREPARING
SULFURIC-ACID BY WET CATALYSIS METHOD
TSYGSA67RFT
CONTACT REACTION RATE Of S02 OXIDATION UNDER PRESSURE
EQUILIBRIUM PRESSURE OF SULFUR-TRIOXIDE VAPORS OVER OLEUMC""
AKSEYV64EPS
REACTOR FOR EXOTHERMIC REACTIONS AT ELEVATED TEMPERATURE AND
PRESSURE BAUMM 66RER
PREPARATION OF SULFURIC-ACID WITHOUT A CATALYST AT HIGH
PRESSURE BURYKA64PSA
IMPROVEMENT OF THE MASS TRANSFER FROM A GAS TO A POROUS
CATALYST OR ADSORBENT BY PRESSURE OSCILLATIONS
ESSO 64IMT
THE CONTACT OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIOXIDE
UNDER PRESSURE GISTAM37TCO
CONTACT OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TR IflXIDE UNDER
PRESSURE LUKVPM33COO
S02 UNDER PRESSURE NOVAS 63SUP
DECOMPOSITION PRESSURES OF NITRATES AND SULFATES
MEASUREMENTS OF SODIUM-VANADATES NEUMB 3SDPO
SOLID CATALYSTS AND REACTION RATES GENERAL PRINCIPLES
HUUGOA43SCA
PRINCIPLES OF REACTOR DESIGN GAS-SOLID INTERFACE REACTIONS
HURTDM43POR
CERTAIN PRINCIPLES OF THE MOTION OF CATALYST PARTICLES IN
INDUSTRIAL VERTICAL PNEUMATIC CONVEYING KURGVM6ACPM
RECOVERY OF VANADIUM FROM THE CATALYST USED IN THF CONTACT
ALBEFM6«ROV
GAS HETEROGENEOUS GAS CATALYSTS
ALDEH SZOPI
OPTIMIZATION OF THE PROCESS OF SULFURIC-ACID PRODUCTION BY
THE CONTACT METHOD AMELAG6600R
PREVENTING THE FORMATION OF SULFORIC-ACIO FOG IN THE CONTACT
PROCESS FOR SULFURIC-ACID MANUFACTURE APAKIA66PFS
PROCESS AND APPARATUS FOR OXIDIZING SULFUR-DIOXI OF
QASSLP17PAA
NOBLE METAL RECOVERY PROCESS •»ERTRj6i>NMR
DESIGN OF CONTACT PROCESS EQUIPMENT WITH AN ADIABATIC
CATALYST LAYER FOR THE OXIDATION OF SULFUR-DIOXIDE DESIGN
OF EQUIPMENT WITH THE INTRODUCTION OF COLD REACTION
MIXTURES AND WITH INTERMEDIATE HEAT EXCHANGERS
BF.SKVS61DOC
ACin PROCESS
DIFFUSION PROCESS
IN
116
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PROCESS
PAGE 82
DETERMINATION OF THE STATIC CHARACTERISTICS Of A CONTACT
REACTOR FOR THE OXIDATION OF SULFUR-DIOXIDE WITH THE AIM
OF OPTIMIZING THE PROCESS BESKVS64DOT
PROCESS DEVELOPMENT IN REMOVING SULFUR-DIOXIDE FROM HOT
FLUE GASES PILOT PLANT STUDY OF THE ALKALIZED
ALUMINA SYSTEM FOR SULFUR-DIOXIDE REMOVAL BIEND 6TPDR
CONTACT PROCESS CONVERTER DESIGN CALDPH53CPC
STUDIES OF THE RATE OF REACTION IN THE VANADIUM CONTACT
SULFURIC-ACID PROCESS CHANHY36SOT
CATALYTIC PROCESS FOR THE MANUFACTURE OF SULFURIC-ACIO IN
SEVERAL CONTACT ANO ABSORPTION STEPS CHEM 66CPF
PRODUCTION OF SULFUR.IC-AC ID BY THE CONTACT PROCESS
FLUE-GAS PROCESS DUNDRH67FGP
OPERATIONAL CONDITIONS IN THE COMBINED CONTACT-CHAMBER
PROCESS ESELIM640CI
USE OF AN IRON CATALYST IN THE CONTACT CHAMBER PROCESS
ESELIM64UQA
SULFUR-TRIOXIDE PROCESS FARB 64STP
INSTALLATIONS FOR INDUSTRIAL GAS CLEANING PROCESS
OPTIMIZATION FOR OPERATING MULTIPLE INSTALLATIONS IN ANY
REGIME FERRG 66IFI
THE PROCESS OF THE OXIDATION OF SULFUR-DIOXIDE WITH
.VANADIUM CATALYSTS5TE ^^^ ^^ FLAH£ ,§!!&?£'*
APPARATut ANDPPROCESSIFOR CIRCULATING POWDERED
CHEMICAL TREATMENT-X
THE DOUBLE CONTACT PROCESS OF
CATALYSTS ?OR ___ ' GENE67CFC
ILID IN
HEMMCE52AAP
SULFURIC-ACIO MANUFACTURE
KAMIY 67DCP
CALCULATION OF THE FLUID!ZED-BED CATALYTIC PROCESS
KERNVSo3C >B
SIGNIFICANCE OF CORROSION TESTING PROCESS WITH SPECIAL
CONSIDERATION OF THE S02 TEST ACCORDING TO DIN-50018
KESTW o5SCT
OPTIMUM CONDITIONS FOR GAS-SOLID CATALYTIC REACTION PROCESS
IN A FIXED-BED KUBOH S90CF
OPTIMUM PROCESS CONDITIONS FOR A COMPLETELY MIXED MULTISTAGE
REACTOR KUBOH 610PC
SULFURIC-ACIO BY CONTACT PROCESS LAMMC 66SAC
OXIDATION OF S02 IN AN APPARATUS WITH A FLUIOI ZED-BED OF FE-
OXIDE CATALYST DURING H2SOA PRODUCTION BY THE CPNISC.T
THER?NFLUENCE OF EXTERNAL DIFFUSION INHIBITION ON THE
PROCESS IN A POROUS CATALYST LEVIVG66T10
CONVERSION STAGE IN THE MANUFACTURE OF SULFURIC-ACID BY
CONTACT PROCESS LOWRGC58CSI
ANTIPOLLUTION PROCESS USES ABSORBENT TO REMOVE
SULFUR-DIOXIDE FROM FLUE-GASES
LUDWS 68APV
PROCESS FOR EXTRACTION OF VALUABLE PRODUCTS FROM SCHISTS
AND OTHER BITUMINOUS FERRUGINOUS AND SULFUROUS SEDIMENTS
ANO COMPOUNDS MANUFACTURED THFREFROM LUPAK 6ftPEV
SULFURIC-ACIO CONCENTRATION PROCESS MANTR 67SAC
10/27/69
PROCESS
PROCESSFS
PAGE
8?
IMPROVEMENTS IN A FLUIOIZED-BED PROCESS MCILAE66IFB
PRODUCTION OF SULFUR-TR I OX IDE BY THE CONTACT PROCESS
A CHEMICAL PROCESS FOR THE PRODUCTION OF OXYGEN ""* 2Pf1S
THE REACTION MECHANISM IN THE CONTACT SULFURIC-ACID PROCESS
AND THE METHOD OF ACTION OF ACTIVATORS NFUMB 29TRM
AMMONIA PROCESS FOR REMOVAL OF SULFUR-DIOXIDE FROM FLUE GAS
NFWAME APR
PROCESS FOR PRODUCING AN ALUMINA CATALYST BASE
HEAT LOSSES TO THE SURROUNDINGS ANO PROCESS STAB IL i
CONTACT-TYPE H2S04 PLANT PETRNM66HLT
RECOVERY PROCESS FOR LOW CONCENTRATIONS OF GASEOUS SULFUR
COMPOUNDS CONTAINED IN RESIDUAL GASES AND FUMES
COLUMBIUM ANO TANTALUM-OXt OES IN THE CONTACT
PRODUCTION OF OLEUM IN THE MANUFACTURE OF SULFUR IC-AC?D3BY°T
THE SHORTENED CONTACT PROCESS REZIIG65POM
ELECTROCHEMICAL PROCESS OF PRODUCING ELECTRICAL ENERGY BY
USING SULFUR-DIOXIDE FUEL AND HALOGEN OXIOANT
S02
MEC
CONVERSION IN THE KACHKAROFF PROCESS
HANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE CONTRIBUTION OF CARBON FREE-RADICALS IN THE
S02 TO S03 OXIDATION PROCESS SIEDJ 65MCO
COMBINATION CONTACT- TOWER PROCESS FOR SULFURIC-ACIO
MANUFACTURE
GAS PURIFICATION PROCESS AND APPARATUS
EFFICIENT SCREENING OF PROCESS VARIABLES
A NEW ABSORPTION PROCESS T
THE BAYER DOUBLE-CONTACT PROCESS FOR CONVERTING SOi
THE BAYER DUAL CATALYST PROCESS
THE ROLE OF VANADYL-SULFATE IN
OXIDATION OF SULFUR-DIOXIDE
REMOVAL OF SULFUR-DIOXIDE FROM FLUF-GASES
GAS PHASE OXIDATION PROCESS
SMYSN167CCT
SOGR 66GPP
5TOWRA66ESP
RNAI62NAP
TO S03
WERTH 64TBO
WERTH 65TBD
RgA£.2f. X«N*P..yk-SULFATE_IN THE PROCESS OF CATALYTIC
WEYCS 55TRC
THE BCR CATALYTIC
ZAWAEA6SROS
CONTACT-CATALYTIC PROCESSES
ALIEVS64CCP
_. _.. IE TO SULFUR-TRIOXIDE AND
THE THEORY OF RAPID CATALYTIC PROCESSES ANDRL 51COC
CATALYTIC OXIDATION TO SULFUR-TPIOXIDE ANO THE THEORY OF
RAPID CATALYTIC PROCESSES II. GENERAL RULF. FOR GAS
DIFFUSION TUBES EFFECT OF DILUTION WITH INERT GASES
EVALUATION OF DRY PROCESSES FOR REMOVING S02 FROM*POWER53CnT
PLANT FLUE GASES BIFNO t-.
ASPECTS IN THE INVESTIGATION OF ADSORPTION AND CATALYTIC
SllPPnRTEOEPLATlNUM METAL CATALYSTS THEr "M ??.-"*! T
METHODS OF USE IN INIJUSTHIAL PROCESSES
THEIR SELECTION AND
118
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PROCESSES
PROCESSING
PRODUCT ION
PAGE 84
OPTIMIZATION OF CATALYTIC PROCESSES IN INDUSTRIAL REACTORS
THE PROBLEM OF EXPERIMENTAL INVESTIGATION OF SEPARATIST"SSii
OF HETEROGENEOUS CATALYTIC PROCESSES OAVTOK58PEI
FLUlnlZED BED PROCESSES JAVOJ 66FBP
DESIGN CALCULATIONS FOR PROCESSES IN FIXED-BEDS AND
FLUlDIZEDrBEOS OF CATALYST KUZIVA65DCF
ACTION OF ULTRASONIC WAVES ON CHEMICAL AND PHYSICOCHEHICAL
PROCESSES LE RA 67AUW
LABORATORY INVESTIGATION OF HETEROGENEOUS CATALYTIC
PROCESSES PAREJN64LIH
HETEROGENEOUS PROCESSES IN RADIATION CATALYSIS
POLALS65HPI
LABORATORY APPARATUS FOR STUDYING CATALYTIC PROCESSES IN
FLUIOIZED-BEDS RODED 68LAS
GAS OR V&POR-PHASE CATALYTIC PROCESSES ROTGH 26GOV
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THE CONCENTRATION OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND 502 OXIDATION
PROCESSES ' SIEDJ 66NCO
DIFFERENCE IN THE OXIDATION PROCESSES OF SULFUR-DIOXIDE
AND HYDROGEN ON A PLATINUM CATALYST UNDER THE CONDITIONS
OF CHILLING ANO THE APPLICATION OF AN ELECTRIC FIELD
STADPM65DIT
SELECTIVITY .FOR SUCCESSIVE FIRST ORDER REACTION AND CATALYST
PORE STRUCTURE DURING HIGH DIFFUSIVE RESISTANCE PROCESSES
TARTR 67SSF
CATALYTIC PROCESSES ON NON-UNIFORM SURFACES TEMKHI49CPO
QUALITATIVE ANALYSIS OF EQUATIONS DESCRIBING EXOTHERMIC
PROCESSES CATALYTIC PROCESS IN A POROUS PLATE
ZELETI660AO
PROCESSING SULFUR-DIOXIDE FROM COMBUSTION GASES
FRANM 64PSD
SULFURIC-ACID PRODUCTION PROCESSING TECHNIQUE DEVELOPMENT
SEFEB 67SAP
SULFUR-TRIOXIDE PROCESSING MESTNG67STP
VANADIUM CATALYZERS FOR THE PRODUCTION OF SULFURIC-ACID
ADADIE35VCF
THE ABSORPTION OF SULFUR-TRIOXIDE IN BUBBLE CAP PLATE
ABSORBERS FOR THE PRODUCTION OF OLEUM AKSEYV64TAO
OPTIMIZATION OF THE PROCESS OF SULFURIC-ACID PRODUCTION BY
THE CONTACT METHOD AMELAG6600R
PRODUCTION ASPEK 64NDI
VANADIUM CATALYZERS FOR SULFURIC-ACID PRODUCTION
BOREGK35VCF
THE OPTIMUM CONCENTRATION OF SULFUR-DIOXIDE IN CONTACT
SULFURIC-ACID PRODUCT ION BOREGK37TOC
SULFUR-TRIOXIDE PRODUCTION WITH OXYGEN RY THE CONTACT METHOD
BOREGK47STP
IMPROVED CATALYST OF HIGH LOAD CAPACITY FOR SULFURIC-ACID
PRODUCTION BUD* 661 CO
113
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PRODUCT ION
PRODUCTION OF A PLATINUM CATALYST
PAGE 85
BUKHSV65POA
NEW CONSTRUCTION MATERIALS FOR APPARATUS IN SULFURIC-ACID
AND SELENIUM PRODUCTION
CONTAMINATION OF A'VANADIUM CATALYST WITH CARBON-BLACK IN
SULFURIC-ACin PRODUCTION BURYKA63COA
PRODUCTION OF SULFUR-TRIOXIDE CHEM 64POS
SOME PROBLEMS CONCERNING SULFURIC-ACID PRODUCTION
CIGDM 64SPC
PRODUCTION OF SULFUR 1C-AC 10 BY THE CONTACT PROCESS
CIMAJ 67POS
PRODUCTION OF SULFUR IC-AC ID FROM FLUE-GAS FROM OIL TREATMENT
DEGTIP66POS
SULFURIC-ACID PRODUCTION FROM ORE ROASTER GASES
DONOJR67SAP
ECONOMICS OF THE PRODUCTION OF SULFURIC-ACI 0 FROM HASTE
SULFUR CONTAINING GASES FEDC1NP65EOT
ALKALINE REGENERATION OF VANADIUM FROM SPENT CATALYST FROM
SULFURIC-ACID PRODUCTION GOLONA66ARO
PRODUCTION OF CATALYSTS IN A FLUIDIZED LAYER FOR OXIDATION
OF SULFUR-DIOXIDE GRADLI62POC
AN AUTOMATIC CONTROL SYSTEM FOR THE DRYING AND ABSORPTION
CYCLE IN SULFURIC-ACID PRODUCTION IGRFV 67ACS
USE OF CERTAIN CATALYSTS ANO ADSORBENTS IN INDUSTRIAL ,
HYGIENE PRACTICE ANO IN PRODUCTION KOTENZ66UOC
PRODUCTION OF SULFURIC-ACID KUZMIN64POS
OXIDATION OF S02 IN AN APPARATUS WITH A FLUIDI ZED-RED OF FE-
OXIDE CATALYST DURING H2S04 PRODUCTION BY THE CONTACT
PROCESS LASTYV6600S
DEVELOPMENT OF CONCEPTS ON REACTION MECHANISM OF
SULFURIC-ACID PRODUCTION MALIIK66DOC
OPTIMU" SHAPES AND SIZES OF ELEMENTS OF A VANADIUM CATALYST
FOR THE PRODUCTION OF CONTACT H2S04 MALKVI640SA
PRODUCTION OF SUFUR IC-AC ID AND OXIDE FROM GAS PURIFICATION
MALTR 63ROS
PRODUCTION OF SULFUR-TRIOXIDE BY THE CONTACT PROCESS
META
PRODUCTION OF SULFUR-TRIOXIDE AND
PRODUCTION OF SULFUR IC-AC
PRODUCTION OF SULFURIC-AC
A CHEMICAL PROCESS FOR TH
SULFURIC-ACID
META
METT
52POS
66POS
65PSA
PRODUCTION OF OXYGEN
MCTTAL65PSA
MUKHIP57ACP
PRODUCTION OF TOWER SULFURIC-ACID BY A PROCEDURE INVOLVING
ACID.CIRCULATION WITH A CROSS-OVER CYCLE NEIPKV64PDT
VANADIUM CATALYSTS FOR THE PRODUCTION OF SULFURIC-ACID
OKAMT 60VCF
PRODUCTION OF SULFURIC-ACID POZIME64PCIS
PRODUCTION OF A GAS OF HIGH SULFUR-TRIOXIDE CONTENT
PROD 65POA
PRODUCTION OF OLFUM IN THE MANUFACTURE OF SULFURIC-ACID 3Y
THE SHORTENED CONTACT PROCESS REZIIG65POM
PRODUCTION OF SULFURIC-ACID RUGHAL65POS
SULFURIC-ACID PRODUCTION PROCESSING TECHNIQUE DEVELOPMENT
SEFEB 67SAP
170
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PRODUCT ION'
PRODUCTS
PROFILES
PROMOTED
PROMOTING
PT
PULP
PULPING
PAGE
CATALYTIC PRODUCTION OF SULFUR-IRIOXIDE SELD ZTCPO
SULFURIC-4CID PRODUCTION WITHOUT COLUMN PACKING
SHEVDM64SAP
CONSTRUCTION MATERIALS FOR FILTERING APPARATUS IN
NICKEL CORALT PRODUCTION SHVAGL63CMF
ELECTROCHEMICAL METHOD OF PRODUCTION OF SULFUR IC-AC ID
SUSHAM63EMO
PRODUCTION
OPTIMUM COMPOSITION OF NITROSE IN SULFURIC-ACI0
RY THE MILLS-PACKARD-PROCESS TSEIAN660CO
SIMULTANEOUS RECOVERY OF SULFUR-DIOXIDE AND THE PRODUCTION
OF NITROGEN FERTILIZERS VASINA60SRS
ELECTROLYTIC PRODUCTION OF SULFURIC-AC ID VASISV50EPO
REMOVAL OF SULFUR FROM PRODUCTS OF COMBUSTION
FRANTT65ROS
ECONOMIC ELIMINATION OF AIR POLLUTION THROUGH RECOVERY
PRODUCTS IN POLYESTER GAS SCRUBBERS HAMPNH65EEA
PROCESS FOR EXTRACTION fTF VALUABLE PRODUCTS FROM SCHISTS
AND OTHER BITUMINOUS FERRUNGINOUS AND SULFUROUS SEDIMENTS
AND-COMPOUNDS MANUFACTURED THEREFROM LUPAK &&PFV
OXIDIZING GASEOUS COMBUSTIBLE WASTE PRODUCTS MICHE 660GC
THE MECHANISM OF CATALYSIS AND A METHOD FOR THE SELECTION
OF CATALYSTS FROM THE POINT OF VI EM OF INTERMEDIATE
PRODUCTS TIKHAV40TMO
ANALYTICAL PREDICTION OF CONCENTRATION AND TEMPERATURE
PROFILES IN A PACKED CATALYTIC TUBE TONES 66APO
KINETIC STUDIES OF THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYSTS PROMOTED RY ALKALI METAL SALTS
7AKHMS58KSO
PROMOTING ACTION OF GROUP-I AND THE LANTHANIDF-GROUP
ELEMENTS ON VANADIUM CATALYSTS BRODKi63PAG
_._ BLUMH 6600P
BOUNDARY LAYER DIFFUSION
DAMAGING OF PT CATALYSTS IN INDUSTRIAL USE
LOSS OF PT02 FROM HEATED PT A --."; '
-ECHAN ISM CHASJC66LOP
ENTROPY OF THE ACTIVE COMPLEX IN THE OXIDATION OF
SULFUROUS-ANHYDRIDE OVER PT CATALYST GOLOGI61EOT
INVESTIGATION OF THE KINETICS OF THE PROCESS!S02*.SOZ-S03)
IN THE STATE OF CHEMICAL EQUILIBRIUM ON A PT CATALYST BY
THE AID OF RAOIOACTIVF S ROITVA62IKP
EFFECTS OF SURFACE ACTIVE IONS ON ABSORPTIVE AND CATALYTIC-
PROPERTIES OF »T AND PO ZAKUGD66EOS
REMOVAL AND RECOVERY OF SULFUR-DIOXIDE IN THE PULP MILL
INDUSTRY GALESF67RAR
SULRJR-DIOXIDE REMOVAL AND RECOVERY FROM PULP MILL POWER
PLANTS
BLEACHED MAGNESIUM-SIJLFITE Pill P
REGENERATION OF MAGNESIUM-B1SULFITE PULPING LIQUOR AND
ABSORPTION OF suLFUR-nioxmr OURING RFGENF.RATION
ROGECE66RMR
GALES
LEKAK
121
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PULVERIZED
PURIFICATION
PURIFYING
PYROSULFATE
QUANTUM
QUARTZ
RAUiATlON
PAGE
87
EFFECT OF FUEL CHARACTERISTICS AND EXCESS COMBUSTION AIR
ON SULFURIC-ACIO FORMATION IN A PULVERIZED COAL-FIRED
BOILER LEE GK67EFC
PURIFICATION OF SULFUROUS RESIDUAL GASES BY ALUMINA BED
SOLUTION TO THE S02 PROBLEM IN AIR PURIFICATION BY °* 6*PSP
OPERATIONAL AND INDUSTRIAL MEASURES BROKW 66STT
AMMONIA RECOVERY FROM WASHINGS OBTAINED DURING THE
PURIFICATION OF SULFUR-DIOXIDE AND SULFUR-TRIOXIDE
CONTAINING GASES CHEM 65ARF
PURIFICATION OF NITROSE EXHAUST GASES GANZSN66PNE
PURIFICATION OF WASTE LIQUIDS AND GASES GEYSK 65POH
PURIFICATION OF SULFUR-DIOXIDE-BEARING GASES AND MANUFACTURE
OF SULFUR-TRIOXIDE HEIMAA32POS
PURIFICATION OF INDUSTRIAL GASES FROM SULFUR-DIOXIDE
KUZNIE66PIG
PURIFICATION OF INDUSTRIAL EXHAUST GASES MALAJ 67POI
PRODUCTION OF SUFURIC-ACIO AND OXIDE FROM GAS PURIFICATION
MALTR 63ROS
PURIFICATION OF SULFURIC-ACID IRON CONTAINING WASHING
DISCHARGES
MULTISTAGE PURIFICATION OF FLUE-GASES
PURIFICATION OF GASFS BY SOLID ADSORPTION
PURIFICATION OF FLUE-GASES FROM SULFUR-DIOXIDE
INDUSTRIAL WASTE-GAS PURIFICATION
PURIFICATION OF GASES FROM
MATAVL67PSA
METT 66MPF
MITS 67POG
RECOVERY OF SULFUR-DIOXIDE _ _
ABSORPTION IN TWO PURIFICATION STEPS
TERiMENTAL LOCAL PURIFICATION OF ~
iUL FUR-DIOXIDE
ROM RESIDUAL GASES BY WET
POTOP 66RSD
HARMFUL ORGANIC AND
INORGANIC DISCHARGES INTO THE ATMOSPHERE AND INTO BODIES
OF WATER ROSCSE66ELP
PURIFICATION OF COMBUSTION GASES SOCI 65POC
GAS PURIFICATION PROCESS AND APPARATUS SOGR 66GPP
PURIFYING A GAS MIXTURE FROM SULFUR-DIOXIDE AMELAG67PGM
A NEW MECHANISM FOR THE ACTION OF THE VANADIUM-PENTOXIDE
SILICA-ALKALI PYROSULFATE CATALYST FOR THE OXIDATION
OF SULFUR-DIOXIDE FRAZJH4DANM
LINEAR FREE-ENERGY.RELATIONSHIPS IN HETEROGENEOUS CATALYSIS
V. AN APPLICATION OF QUANTUM CHEMICAL REACTIVITY INDEXES
TO HETEROGENEOUS CATALYSIS MOCHI 67LFE
CATALYTIC OXIDATION OF SULFUR-DIOXIDE ON HEATED QUARTZ
SURFACES FLIND 5 1C00
THFRMAL RADIATION AND CHEMICAL STABILITY OF SULFUR-DIOXIDE
BFNNRL63TRC
PROSPECTS FOR NUCLEAR RADIATION APPLICATION IN CATALYSIS
CIBDS 65PFN
122
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RADIATION
RADIATIONS
RADIOACTIVE
RATE
PAGE
88
PROSPECTS FOR NUCLEAR RADIATION APPLICATION IN CATALYSIS
CIBOS 67CNR
EFFECT OF NUCLEAR RADIATION ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE REACTION OF S02 OXIDATION KOZAZ 66EON
RADIATION EFFECTS ON SOL D CATALYSTS ONO S 63RAS
HETEROGENEOUS PROCESSES IN RADIATION CATALYSIS pOL4LS65HPI
EFFECT OF IONIZING RADIATIONS ON THE SULFUR-DIOXIDE-OXYGEN
SYSTEM II THE OXIDATION OF SULFUROUS-AC10 TO SULFURIC-ACID
BY ACTION OF X-RAY RADIATION SCHRR 64EOI
RADIATION CATALYSIS SELIM 67RC
HETEROGENEOUS RADIATION CATALYSIS SPITVI64HRC
HETEROGENEOUS RADIATION CATALYSIS AND RADIOACTIVE CATALYSIS
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INFLUENCE Of RADIATION REACTIVITY AND CATALYTIC ACTIVITY OF
3S TAYLEH64IRR
THI
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ECTS OF RADIATION ON CATALYSTS
TODON 66TEO
EFFECT OF IONIZING RADIAT IONS ON THE SULFUR-DIOX IDE-OXYGEN
SYSTEM li'THE'OXlbAfiON OF SULFUROUS-ACIO TO SULFURIC-ACID
BY ACTION OF X-RAY RADIATION ' "
SCHRR 64EOI
POSSIBLE MECHANISM OF THE EFFECT OF RADIOACTIVE ADDITIONS
ON THE CATALYTIC AND CHEMI SORPTl VE PROPERTIES OF
SEMICONDUCTORS BARUVG65PMO
SULFUR-OXIDE REACTIONS RADIOACTIVE SULFUR AND "ICROPROBE
STUDIES OF CORROSION AND DEPOSITS KRAUHH68SOR
INVESTIGATION OF THE KINETICS OF THE PROCESS(S02*.SO?=S03>
IN THE STATE OF CHEMICAL EQUILIBRIUM ON A PT CATALYST BY
THE AID OF RADIOACTIVE S ROITVA62IKP
EFFECT OF RADIOACTIVE COMPOUNDS ON CATALYTIC OXIOATION^OF..^
CATALYSIS AND RADIOACT, VE
SPI T VI 66HRC
CONTACT REACTION RATE OF S02 OXIDATION UNDER PRESSURE
ABE K 60CRR
EFFECTIVENESS FACTORS FOR GENERAL REACTION RATE FORMS
BI SCKB65EFF
CALCULATION OF THE RATE OF REACTION CONSTANTS IN TH
OXIDATION OF S02 TO S03 ON A VANADIUM CATALYST
LACK OF DEPENDENCE OF CONVERSION ON FLOW RATE IN CATALYTIC
STUDIES CHAMRP66LOD
STUDIES OF THE RATE OF REACTION IN THE VANADIUM CONTACT
SULFURIC-ACIO PROCESS CHANHY36SOT
KINETIC STUDIES ON THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYSTS III. A COMPARISON OF THE RATE EQUATIONS
OBTAINED WITH SOME INDUSTRIAL VANADIUM CATALYSTS
EFFECT OF TEMPERATURE ON THE RATE OF FORMATION OF SULFURIC
BY THE OXIDATION OF SULFUR-DIOXIDE ON ACTIVATED CARBON BY
THE LIQUID CONTACT METHOD DAVTOK61ETR
123
10/27/69
KATE
1ATES
PAGE
THE RATE OF OXIDATION OF SULFUR-DIOXIDE «ITH A CCHKESClfcL
VANADIUM CATALYST EKLURB57TRO
DETERMINATION OF THE RATF OF CONVERSION OF SULFUR-DIOXIDE
INTO SULFUR-TRIOXIDE FIALGM6000T
TEMPERATURE RELATION FOR THE RATE OF OXIDATION OF
SULFUR-DIOXIDE ON VANADIUM CATALYSTS
CALCULATION OF THE RATE OF A HALF ORDER REACTION
CONTACT REACTION RATE OF S02 OXIDATION
THE RATE BY A DIFFERENTIAL METHOD
ACTION RATE OF SO2 OX1DAT1
HARAH 59CRM
APPLICATION OF THE
EV56TRF
TN PORES OF A CATALYST' ' " GLASV 66COT
MEASUREMENT OF CATALYTIC OXIDATION RATE OF SULFUR-DIOXIDE
HARAH 57MOC
DETERMINATION OF
CONTACT RE ACT ION'RATE OF" SO2 OXIDATION MEASUREMENT OF""
THE RATE OF FOUR DIFFERENT FEED GASES ~
CONTACT REACTION RATE OF S02 OXIDATION _. _. .
RATE EXPRESSION TO NEW OBSERVATIONS AND ILLUSTRATION FOR
THE CONVERTER DESIGN HARAH 59CRR
DIFFUSION AND REACTION RATE HARAY 63DRR
THE EFFECT OF HIGH CONCENTRATIONS OF SULFURIC-ACID ON THE
RATE OF OXIDATION Of SULFUR-DIOXIDE IN THE PRESENCE OF
BIVALENT MANGANESE IONS KASHLI36TEO
EFFECT OF THE EXTERNAL SURFACE ON THE REACTION RATE AND
SELECTIVITY OF ISOTHERMAL CATALYST PARTICLES
KRAMSJ66EOT
THE RATE OF OXIDATION OF S02 WITH INDUSTRIAL VANADIUM
CATALYST KUBOH 59TRO
INFLUENCE OF REACTION RATE ON OPERATING CONDITIONS IN THE
CONTACT SULFURIC-ACIO MANUFACTURE LEWIWK25IOR
INCREASED PRECIPITATION RATE OF ELECTROSTATIC SEPARATORS
THE INTERPRETATION OF INITIAL RATE DATA WITH THE
HOUGEN-WATSON MODELS
THE CORROSION RATE OF CAST IRON BY SULFUR-DIOXIDE
META
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MEZAR 67TIO
NAKAY 66CRC
BE
RATE OF ABSORPTION OF SOLUBLE GASES IN A NETTED WALL TUBE
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RAMMVM65RAS
SEMICONDUCTANCE AND CATALYSIS RELATION BETWEEN
CATALYTIC ACTIVITY, STOICHIOMETRIC COMPOSITION
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QfLEk!CJ.RpN_LINK.AGE.FOR ^CONDUCTING MI _XEp.CATALYSTS~bF
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THE HOPCALITE-TYPE III. RELATION BETWEEN CATALYTIC
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LINKAGE FOR P-CONOUCTING MIXED CATALYSTS OF THE HOPCALITE
TYPE __ RIENG 6*SAC
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ALGEBRAIC MANIPULATIONS OF THE PATE EQUATIONS OF CERTAIN
CATALYTIC REACTIONS WITH A DIGITAL COMPUTER
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OVERALL RATE OF CATALYTIC REACTIONS AS INFLUENCED BY THE
INHOMOGFNEITY OF THE FLUIDIZED BED TDDEOM6*
DETERMINATION OF THE ACTUAL RATE OF OXIDATION OF
SULFUR-DIOXIDE WEYCS 6"5DOT
REACTION RATES OF CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH
VANAOIUM-PENTOXIDE CATALYSTS HARAH 59RRO
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12k
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"ATES
REACTION
PAGE
STL in CATALYSTS AND REACTION RATES GENERAL PRINCIPLES
HOUGOA43SCA
SCLIO CATALYSTS AND REACTION RATES OXIDATION OF SULFUR-
DIOXIOE IJYEHOA43SDA
CONTACT REACTION RATE OF S02 OXIDATION UNDER PRESSURE
ABE K 60CRR
DIFFUSION AND HETEROGENEOUS REACTION EFFECT OF
DIFFERENT CATALYST GEOMETRIES ABLOCM650HR
THE DYNAMICS AND CONTROL OF AN EXOTHERMIC REACTION IN A
FLUIDIZEO-BED REACTOR BARNLA&5TDA
PF ACT ION KINETICS IN A TUBULAR REACTOR BAROT 52RKI
DESIGN OF CONTACT PROCESS EQUIPMENT WITH AN ADIABATIC
CATALYST LAYER FOR THE OXIDATION OF SULFUR-DIOXIDE DESIGN
OF EQUIPMENT WITH THE INTRODUCTION OF COLO REACTION
MIXTURES AND WITH INTERMEDIATE HEAT EXCHANGERS
BESKVS63DOC
EFFECT IVEMESS FACTORS FOR GENERAL REACTION RATE FORMS
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INITIATING A HOMOGENEOUS REACTION IN A GAS BY SOLID CATALYST
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?.ELATmNEBETHEEN.REACTION_gRDER AND FNERGY OF ACTjyATION.
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AND INVERSE REACTIONS BORERKfcSRHP
[IN OF THE RATE HF REACTION CONSTANTS IN THE
DN OF S02 TO SO3 ON A VANADIUM CATALYST
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STUDIES OF THE RATE OF REACTION IN THE VANADIUM CONTACT
SULFURIC-ACID PROCESS CHANHY36SOT
OXIDATION OF SULFUR-DIOXIDE BY PHOTOCHEMICAL REACTION AND
PHOTOSENSITIZATION CHENSW58OOS
EXOTHERMIC GAS REACTION SUCH AS OXIDIZING SULFUR-DIOXIDE TO
TRIQXIDE CLARC92TEGR
THE REACTION OF S02 AND 02 IN AQUEOUS SOLUTIONS ON MNS04
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HFAT TRANSFER ANALOGY FOR DIFFUSION AND FIRST ORDER CHEMICAL
REACTION IN A CATALYST PORF. COUGRH67HTA
MASS TRANSPORT AND CHEMICAL REACTION IN MULTIFUNCTIONAL
CATALYST SYSTFMS OUNNDJ65MTA
EFFECT OF rfATER VAPORS ON THF REACTION OF SODA WITH
SULFUR-DIOXIDE AT TEMPERATURFS ABOVE 100-DEGRFES
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CONTROL OF TEMPERATURE BY aDMIMS I"N OF A COLD COMPONENT AS A
MEANS FOR ENSURING OPTIMAL CONDITIONS FOP AN EXOTHERMIC
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CALCULATION OF THE RATE OF A HALF ORDER REACTION PROCEEDING
IN PORES OF A CATALYST GLASV 6SCOT
CONTACT REACTION RATE OF SD2 OXIDATION ~
THF RATE BY A DIFFERENTIAL MF THOD
CfNTACT REACTION RATE OF S02 OXIDATION
THE RATE OF FOUR DIFFERENT fTF.n f.ASFS
CCMTACT REACTION RATE OF S02 OXIDATION
BITE EXPRESSION TO N"=W OHSERVA1IHNS AND
FHF CONVERTER OFSIGN
DETERMINATION OF
HARAH S8CRR
MEASUREMENT OF
HARAH 59CRM
APOL ICATION OF THF
ILLUSTRATION FOR
HARAH "59CRP
10/77/69
REACTION
PAGE
REACTION RATES OF CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH
VANAOIUM-PENTOXIDE CATALYSTS HARAH 59RRO
DIFFUSION AND REACTION RATE HARAY 630RR
MODELLING OF CHEMICAL REACTORS HEAT AND MASS TRANSFER WITHIN
A POROUS CATALYST PARTICLE SOME RESULTS OF AN ANALYSIS
FOR A ZERO-ORDER REACTION HLAVV 67MOC
SOLID CATALYSTS AND REACTION RATES GENERAL PRINCIPLES
HOUGOA43SCA
REACTION OF SULFUR-DIOXIDE WITH ACTIVE NITROGEN
JACOA 66RSD
ULTRASONICALLY ACTIVATED CATALYSTS FOR CHEMICAL REACTION
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OVERALL CATALYTIC EFFECTIVENESS FACTORS AND THEIR SHAPE
CORRELATIONS WITH MASS TRANSFER AND REACTION ON THE
EXTERNAL SURFACE KASAS 67OCE
EFFECT OF NUCLEAR RADIATION ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE REACTION OF SO2 OXIDATION KOZAZ 66EON
EFFECT OF THE EXTERNAL SURFACE ON THE REACTION RATF AND
SELECTIVITY OF ISOTHERMAL CATALYST PARTICLES
KPAMSJ66EOT
OPTIMUM CONDITIONS FOR GAS-SOLID CATALYTIC REACTION PROCESS
IN A FIXED-BED KUBOH S90CF
TEMPTS TO INCREASE THE THERMAL RESISTANCE OF THE
'- ~- OF OXIDATION
_. KUCZW 59ATI
KINETICS OF SORPTION AND OF THE CHEMICAL REACTION ON A
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REACTION
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10/27/49
PEACT IONS
PAGE 93
APPARATUS FOR AFFECTING GAS REACTIONS BY MEANS OF ELECTRICAL
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KEACTOR
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PAGE 95
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PAGE 99
REGENERATION AND REACTIVATION OF A PLATINUM REFORMING
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SCRUBBERS
SCRUBBING
GAS ABSORPTION BY MULTISTAGE VENTURI SCRUBBERS
PAGE 100
VOLGBP64GSM
_______ ______
FROM CONTACT SULFURIC-ACID INSTALLATION
SCRUBBING OF SULFUR-DIOXIDE FROM FLUE-GASES
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USE OF A SULFUR-DIOXIDE
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SELECTIVITY
EFFECT OF IRREGULAR PORES ON THE
THE INFLUENCE OF SURFACE COVERAGE ON CATALYTIC EFFECT
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AND SELECTIVITY
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ACT I
SELENIUM
SEMICONDUCTANCE
STRUCTION MATERIALS
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ITY STOICHIOMETRIC COMPOSITION AND RATE OF ELECTRON
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SCRUBBING AND UTILIZATION OF EXHAUST GASES FROM METALURGICAL
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SEMICONDUCTOR
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MECHANISM OF THE CATALYTIC OXIDATION OF so? CONSIDERED
FROM THE THEORY OF SEMICONDUCTOR CORRECTION OF THF
MECHANISM OF CALDERRANK KAWAT 54TPP
OXIDATION OF SULFUR-DIOXIDE BY N-TYPE SEMICONDUCTOR CATALYST
ORIGIN OF THE COMPENSATION EFFECT IN CHEMICAL REACTIONS
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SEMICONDUCTORS BARUVG65PMO
THE CHARGE TRANSFER THEORY OF GAS-SURFACE INTERACTIONS AND
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SEMICONDUCTORS AND CATALYSIS LOEBE 6ISAC
EFFECTIVENESS FACTORS OF CATALYST PARTICLES WITH SHAPE
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EFFECTIVENESS FACTORS OF CATALYST PARTICLES WITH SHAPE
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EFFECT OF INTERNAL DIFFUSION ON CATALYTIC REACTIONS
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OPTIMUM SHAPES AND SIZES OF ELEMENTS OF A VANAOIUM CATALYST
FOP THE PRODUCTION Of- CONTACT H2S04 «ALKVI6«OSA
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OF
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136
135
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SILICA-GEL
SILICA-GELS
SILICEOUS
S/LICIC-ACID
SILICON
SILICON-
SILVER
SIMULATION
SIZE
SIZES
SLAGGING
PAGE 102
OXIDATION OF S02 BY 02 OR 02-03 MIXTURE IN THE PRESENCE OF
SILICA-GEL ADSORPTION OF 02 ON SILICA-GEL ALUMINA-GEL AND
COTTON BRINE 43QOS
EFFECT OF A POROUS SILICA-GEL CATALYST CARRIER ON THE
VELOCITY OF OXIDATION OF SULFUR-DIOXIDE GAS :
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SILICA-GEL GPAS 36SG I
SILICA-GEL CATALYSTS MALAJ 35SGC J
MACROPOROUS CATALYST CARRIERS OF SILICA-GEL OR
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PLATINIZED SILICA-GELS AS CATALYSTS FOR THE OXIDATION
OF SULFUR DIOXIDE HOLMHN29PSG
DEPOSITING METALS ON SILICEOUS CATALYST SUPPORTS FROM AMINE
COMPLEXES IN AQUEOUS AMMONIA SOLUTIONS MULABF67DMS
MECHANISM OF OXIDATION OF SULFUR-DIOXIDE IN THE PRESENCE
OF ACTIVATED VANADIUM CATALYSTS INFLUENCE OF AN
ADMIXTURE OF SALTS OF ALKALI ELEMENTS AND AMORPHOUS
SILICIC-ACID
ROREGK4QMOP ;
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SULFUR-TRIOXIDE SYNTHESIS USING
IRON-OXIDE CATALYST ON A SILVER CARRIER SCHWGM67IMC
INVERS MIXED CATALYSTS
IRON-OXIDE CATALYST
SIMULATION AND OPTIMIZATION OF CHEMICAL REACTORS
BOREGK65SAO
DEPENDENCE OF THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE ON
THE PARTICLE SIZE OF THE CATALYST IN AGITATED AND
FIXED-BEDS SCHYF MOOT
OPTIMUM SHAPE AND SIZE OF CATALYST GRAINS SIINMG640SS
OPTIMUM SHAPE AND GRAIN SIZE FOR A VANADIUM CATALYST
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THE EFFECT OF GRAIN SIZE ON CATALYST PERFORMANCE
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ACTIVITY IN THE FLUID! ZED-BED OXIDATION OF SULFUR-DIOXIDE
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FOR THE PRODUCTION OF CONTACT MZSO* M&LKVI640SA
CHEMICAL REACTIONS IN THF CO«fUIST| UN SPACE OF SLAGGING
BOILERS HICKK -!7CRI
10/27/69
SNPA'S
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AIR
PROCESS FOP. H2Sn'i
POLLUTION
PAGE 103
"RDOUCTION DEVELOPED WITH EYE ON
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EFFECT OF WATER VAPORS ON THF _ _ ._.
SULFUR-DIOXIDE AT TEMPERATURES ABOVE
REACTION OF SODA WITH
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HERBG 66EHS
DECOMPOSITION PRESSURES OF NITRATES AND SULFATES
MEASUREMENTS OF SOD IUM-VANAOATES
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CONTACT OF FLUIDIZABLE SOLIDS WITH GASEOUS FLUIDS
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CATALYSIS UNDER IRRADIATION IN THE PRESENCE OF
FOR SUBDIVIDING PARTICULATE
SOL IDS COEKR 63CU1
METHOD AND APPARATUS FOR SUBDIVIDING PARTICULATE SOLIDS
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A CATALYTIC REACTOR
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SOLIDS TAYLEH64IRR
THE SOLUBILITY OF S02 IN WATER
SOLUBILITY OF SULFUR-DIOXIDE IN WATER
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STABILITY OF FINELY DISPERSED POROUS BODIES CATALYSTS AND
SO'BENTS SCHf.F.OftSSPP
KINETICS OF SORPTION
UNIFORM-SURFACE CATALYST
AND Cf THE CHEMICAL REACTION ON A
TALYST IN A FLUID! ZED BED INVOLVING
COMPLETE INTERMIXING OF PARTICLES AND OF THE GAS
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SORPTION PROPERTIES OF SUPPORTED PDTASSIUM-VANADATF CATALYST
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137
138
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10/27/69
PAGE
10/27/&9
PAGE 105
SH3
CALCULATION OF THE RATE OF REACTION CONSTANTS IN THE
OXIDATION OF S02 TO SOT ON A VANADIUM CATALYST
BUPYKA63COT
INCREASE OF THE YIELD OF SOT IN THE CATALYTIC OXIDATION OF
Sfl2 HOEHH 671 OT
CATALYTIC CONVERTER SUITABLE FOR OXIDIZING S02 TO S03
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CONTACT PROPERTIES HF CHROMIUM-OXIOE-STANNIC-OXIOE CATALYSTS
FOR THE OXIDATION OF S02 TO S03 KURINP56CFO
S03 AND SULFURIC-ACIO BY CATALYTIC CONVERSION OF GASES
CONTAINING S02 METT 66SAS
SPECTROGRAPHIC
SPECTROMETRY
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RATE OF ABSORPTION -- ... - —. -
ABSORPTION OF S03 BY SULFURIC-ACID-MONOHYDRATE
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CATALYTIC CONVERTER FOR OXIDIZING S02 TO S03 RIDDES39CCF
THE ELECTRONIC MECHANISM OF THE CATALYTIC FORMATION OF S03
SCHWGM63EMC
ELECTRONIC MECHANISM OF THE CATALYTIC 503 FORMATION ON CR203
CONTACTS SCHWGM64EMC
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CAPBON
THE CONTRIBUTION OF CARBON FREE-RADICALS IN THF
S02 TO S03 OXIDATION PROCESS SIEDJ 65MCO
— PROCESS FOR CONVERTING S02 TO SO3
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THE BAYER DOUBLE-CONTACT
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MASS SPECTROMETRY OF MATERIALS PRODUCING SULFUR-TRIOXIDE
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FORMATION OF SULFUR-TRIOXIOE APPLICATION OF INFRARED
SPECTROMETRY TO FUNDAMENTAL STUDIES LADNWR63FRT
THE KINETICS OF REACTION BETWEEN OXYGEN ATOMS AND
S02 AN INVESTIGATION BY ELECTRON-SPIN-RESONANCE
SPECTROMETRY MULCMF67KRO
CATALYTIC OXIDATION OF SULFUP-DIOXIDE BY HEAVY HYDROGEN
ON THE SURFACE OF A PLATINUM SPONG"
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ON A PLATINUM SPDNGF
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SPRAY COOLER TUBES IN SULFURIC-ACIl) MANUFACTURE
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CERAMIC CATALYST HAVING
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CARRC 66MST
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THERMAL RADIATION AND CHEMICAL STABILITY OF SULFUR-DIOXIDE
STABILITY Of BATCH CATALYTIC FLUIDIZED-BEDS LUSSDL6lsOB
HEAT LOSSES TO THE SURROUNDINGS AND PROCESS STABILITY OF A
CONTACT-TYPE H2S04 PLANT °ETRNM66HLT
SOME PROBLEMS IN THE PHYSIOCHEMICAL THEORY OF THE
STABILITY OF FINELY DISPERSED POROUS BODIES CATALYSTS AND
SORBENTS SCHCED6SSPP
STABILIZING LIQUID SULFUR-TR IOXIDE WITH PHOSPHORUS
CONTAINING COMPOUNDS
STABILIZING SULFUR-TR[OXIDE
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ACTIVITY OF THERMALLY STABLE VANADIUM CATALYSTS FOR THF
OXIDATION OF SULFUR-DIOXIDE KUNITI63AOT
A MECHANICALLY STABLE IRON CATALYST FOR THE OXIDATION OF
SULFUR-DIOXIDE MUKHIP64AMS
THE EFFECT OF THE CONCENTRATIONS OF IMPREGNATING SOLUTIONS
UPON THE CHEMICAL COMPOSITION AND STRUCTURE OF A
MECHANICALLY STABLE VANADIUM CATALYST MUKHIP65TEO
STABLE AND UNSTABLE BEHAVIOR OF ADIABATIC TUBULAR REACTOR
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STANNIC-HYDROXIDE
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CHRIDH66STM
CORROSION OF~CHEH1CAltY"RESlSTANT"CHRbMiUM"N~--HE
IN A SOOIUM-SULFATE SOLUTION ACIDIFIED WITH
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THE VARIATION WITH TEMPERATURE OF THE CATALYTIC ACTIVITY
OF AN OXIDIZED STAINLESS STEEL SURFACE IN THE OXIDATION
OF SULFUR-DIOXIDE JACKPJ59VTC
EFFECT OF S02 GAS ON PITTING CORROSION OF AUSTENTIC
STAINLESS STEEL MORIS 65ESG
MAKING ACID IN IRON AND STEEL EQUIPMENT RINCJB67MAI
STEELS FOR DIFFICULT CORROSION CASFS IN THE CHEMICAL
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STEELS IN SULFURIC AND EXTRACTION PHOSPHOR IC-ACI OS
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EFFECT OF SULFUR-DIQXIDE ON THE ATMOSPHERIC CORROSION OF
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EFFECT OF HIGH TEMPERATURE PLASTIC DEFORMATION AND
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OXIDATION OF AMMONIACAL SULFUR-DIOXIDE SOLUTION WITH
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STRUCTURAL CHARACTERIZATION OF CATALYSTS
OF MERCURY
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..1-39
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10/27/69
STRUCTURAL
STRUCTURE
STRUCTURES
SUBLIMATION
SUFURIC-ACID
SULFATES
STRUCTURAL CHARACTER UAT ION OF CATALYSTS
OF DATA ON GAS ABSORPTION
PAGE 106
INTERPRETATION
ASENJ 67SCP
POROUS STRUCTURE OF ADSORBANTS AND CATALYSTS OUBIMM66PSA
ACTIVITY STRUCTURE AND ELECTRICAL PROPERTIES OF MIXED
VANADIUM CATALYSTS EZHK2I64ASA
A COMPUTATIONAL MODEL FOR THE STRUCTURE OF POROUS MATERIALS
EMPLOYED IN CATALYSIS FOSTRN66ACM
EFFECT OF STRUCTURE OF REACTING MOLECULES ON REGULARITIES
OF THEIR CATALYTIC TRANSFORMATION • GOROYR66EOS
SURFACE STRUCTURE OF KIESELGUHR CARRIERS AND CATALYSTS FOR
THE OXIDATION OF SULFUR-DIOXIDE JIRUP 57SSO
PORE STRUCTURE AND GASEOUS DIFFUSION IN SOLID CATALYSTS
JOHNNF65PSA
PORE STRUCTURE AND GASEOUS DIFFUSION IN SOLID CATALYSTS
JOHNMF65PSG
ELECTRON-MICROSCOPIC STUDY OF THF POROUS STRUCTURE OF A
VANADIUM CATALYST FOR SC2 OXIDATION KARA0865EMS'
THE STRUCTURE AND
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MPSSRL66SAH
THE STRUCTURE OF SUPPORTED PLATINUM CATALYSTS EXAMINATION
BY ELECTRON MICROSCOPY MOSSR167SSP
SOME RESULTS OF A STUDY OF THE STRUCTURE OF A WEAR-RESISTANT
VANADIUM CATALYST MUKHIP65RSS
THE EFFECT OF THE CONCENTRATIONS OF IMPREGNATING SOLUTIONS
UPON THE CHEMICAL COMPOSITION AND STRUCTURE OF A
- ""ABLE VANAO
HUM CATALYST
MUKHIP65TEC1
MECHANICALLY STABL.
STRUCTURE OF WEAR RESISTANT VANADIUM CATALYSTS FOR
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MUKHIP67SWR
RELATION BETWEEN REACTIVITY AND STRUCTURE OF METALLIC
SURFACES SANDJV64RRR
PORE STRUCTURE IN CATALYSTS TARTP 66PSC
SELECTIVITY FOR SUCCESSIVE FIRST ORDER REACTION AND CATALYST
PORE STRUCTURE DURING HIGH DIFFUSIVE RESISTANCE PROCESSES
TARTR 67SSF
INDUSTRIAL EFFECTIVENESS
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RELATION BFTWEEN CATALYTIC ACTIVITY OF SflUE METALS AND THEIR
SUBLIMATION HEATS RFSHSM66RBC
PRODUCTION OF SUFURIC-ACID AND OXIDE FROM C,AS PURIFICATION
MALTR 61POS
THE EFFECT OF ALKALI «ETAL SULFATFS ON THh CATALYTIC
PROPERTIES OF VANADIUM DMSAP&1TEC1
EFFECT OF ALKALI METAL SULFATES ON THF ACTIVITY OF
V2O5 FOR THE CATALYTIC nxIDATION OF SULFUR-DIOXIDE
JIRUP 6 IF. AM
EFFECT OF THE ALKALI .METAL SULFATES ON THF ACTIVITY OF
VANAOIUM-PENTnxiOE IN THE CATALYTIC OXIDATION OF
SULFUR-OX I OF JIPUP 61EOT
10/77/69
SULFATES
SULFUR
PAGF 107
EFFECT OF THE ALKALI MF.TAL SULFATES ON THE ACTIVITY OF
VANADIUM-PENTOXIOE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE JIRUP 63VPC
DECOMPOSITION PRESSURES OF NITKATCS AND SULFATES
MEASUREMENTS OF SOD IUM-VANADATES NFUMB 3SDPO
SULFUR SMOKE REMOVAL SYSTEM BOUVRF64SSR
ISOTOPE EFFECT OF SULFUR DURING THE OXIDATION OF
S02 IN SULFURIC-ACIO AND THE MECHANISM OF THIS
OXIDATION COURP 6*>IES
RECOVERY OF SULFUR FROM FLUE-GAS BY THE USE OF AMMONIA
CRAXSRS2RSF
INVESTIGATION OF THE MECHANISM OF OXIDATION HYDROGENATION
AND ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS
OXIDATION OF SULFUR DIOXIDE ON ACTIVATED CARBON AT 20-OEG
IN THE PRESENCE OF WATER VAPOR DAVTOK61IMO
ECONOMICS OF THE PRODUCTION OF SULFURIC-AC ID FROM WASTE
SULFUR CONTAINING GASES FEOONP65EOT
RECOVERY OF SULFUR FROM INDUSTRIAL GASES FIVE 66ROS
REMOVAL OF SULFUR FROM PRODUCTS OF COMBUSTION
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REMOVAL OF SULFUR COMPOUNDS FROM FLUE-GASES GRILW 66RSC
SULFUR-OXIDES AND OTHER SULFUR COMPOUNDS A BIBLIOGRAPHY WITH
ABSTRACTS GROSA 6SSOA
OXIDATION OF SULFUR-DIOXIDE TO SULFUR TRIOXIDE
HIMSFR4900S
PLATINIZED SILICA-GELS AS CATALYSTS FOR THE OXIDATION
OF SULFUR DIOXIDE HOLMHN29PSG
CORROSION RESISTANCE OF CR-NI WELDS IN ATMOSPHERES
CONTAINING SULFUR COMPOUNDS KALUF 65CRC
INFLUENCE OF CATALYSIS CONDITIONS ON CONTENT OF SULFUR IN
BARIUM-ALUMINUM-VANADATE CATALYST DURING THE OXIDATION OF
SULFUR-DIOXIDE KORNGP56IOC
SULFUR-OXIDE REACTIONS RADIOACTIVE SULFUR AND MICROPRORE
STUDIES OF CORROSION AND DEPOSITS KRAUHH6BSOR
SULFUR CHEMISTRY AND ITS ROLE IN CORROSION AND DEPOSITS
LEVYA 63SCA
REGENERATION OF SULFUR CONTAINING COMPOUNDS FROM BURNED
GASES MOMS 65ROS
MANUFACTURE OF SULFUR FROM GAS CONTAINING SULFUR-DIOXIDE
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METHODS OF REDUCING EMISSION OF OXIDES OF SULFUR FROM COAL
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SULFUR OXIDATION WITH INTERNAL HEAT EXCHANGE PETRNN47SOW
RECOVERY PROCESS FOR LOW CONCENTRATIONS OF GASF.OUS SULFUR
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THE SIMULTANEOUS ABSORPTION OF SULFUR-OXIDES AND ONE OR MORE
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CATALYTIC REMOVAL OF SULFUR COMPOUNDS FROM GASES
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NEW CATALYST FOR THE RECOVERY OF GASEOUS SULFUR COMPOUNDS
AND THEIR TRANSFORMATIONS INTO SIILFUR-TRIOXI DE
TERMR 64NCF
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10/?7/h9
SULFUR
SULFUR-OXIDE
SULFUR-OXIDES
PAGE 10R
METHODS OF REDUCING EMISSIONS (IF OXIDES OF SULFUP FROM COAL
U.S.DE65MRE
SULFUR-OXIDE REACTIONS JENKJR63SOP.
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVITY OF
VANADIUM-PENTOXIDE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE ' JIRUP 63EOT
EFFECT OF THE ALKALI METAL SULFATFS ON THE ACTIVITY OF
VANADIUM-PENTOXIOE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE JIRUP 63VPC
SULFUR-OXIDE REACTIONS RADIOACTIVE SULFUR AND MICROPROBE
STUDIES OF CORROSION AND DEPOSITS KPAUHH68SOR
INTERACTIONS IN SULFUR-OXIDE IRON-OXIDE SYSTEMS
CON'TR'OL' OF S\JLF"UR-OX'IDE POLLUTION LUDwjH67cns
REMOVAL OF SULFUR-OXIDES FROM THE RASES CORBPF52ROS
PROBLEMS AND POSSIBILITIES OF MAINTAINING ATMOSPHERE FREE
OF SULFUR-OXIDES DRATH 67PAP
SULFUR-OXIDES AND OTHER SULFUR COMPOUNDS A BIBLIOGRAPHY WITH
GROSA 65SOA
HAMPG 62SSO
KRIZM 65SOR
ABSTRACTS
SEPARATION OF SULFUR-OXIDES FROM WASTES GASES
SULFUR-OXIDES REMOVAL FROM FLUE-GASES
INDUSTRIAL GASES
REMOVAL OF SULFUR-OXIDES FROM
OTTO 57RSO
THE SIMULTANEOUS ABSORPTION OF SULFUR-OXIDES AND ONE OR MORE
REDUCED SULFUR COMPOUNDS FROM INDUSTRIAL GASES ESPECIALLY
FLUE-GASES REINLU65SAS
REDUCTION OF AMBIENT 4IP CONCENTRATION OF SULFUR-OXIDES
— - SPAIPW66ROA
SULFUR-TRIOXIDE
PRESENT AND FUTURE PROSPECTS
SULFUR-OXIDES IN FLUE-GAS AND IN THE ATMOSPHERE
KEEPING THE AIR PURE
RECOVERY OF SULFUR-OX IRES FROM STACK GASES
A PROBLEM OF
SPENG 65SOI
TF.LLAJ68ROS
ACHIC «9ST
SULFUR-TRIOXIDE .
UTILIZING WASTE FROM THE ALUMINUM-CHLORIDE INDUSTRY FOR
CARRIERS OF PLATINUM IN THE OXIDATION OF SULFUR-DIOXIOE TO
SULFUR-TRIOXIDE AOADIE34UWF
EQUILIBRIUM PRESSURE OF SULFUR-IP 10X1DE VAPOKS OVER PLEUM
AKSEYV64FPS
THE ABSORPTION OF SULFUR-TRIOXIDE IN BUBBLE CAP PLATE
ABSORBERS FOR THE PRODUCTION PF OLEUM AKSEYVIS4TAO
OXIDATION OF SULFUR-DIOXIDF TO SULFUR-TRIOXIDE
AKTI 2200S
CATALYTIC OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIOXIDE AND
THE THEORY OF RAPID CATALYTIC PROCESSES ANDRL 51TOO
CATALYTIC OXIDATION TO SULFUR-IP I OXIDE AND THE THEORY OF
RAPID CATALYTIC PROCESSES n. GENERAL RULE FOR GAS
DIFFUSION TUBES EFFECT OF DILUTION WITH INERT GASES
ANDPL 13COT
GASES CONTAINING SULFU*-TK MIX Inf BADI 54GCS
VANADIUM CATALYST FOR nxiDAFIPN OF SULFUR-DIflX IDF TO
SULFUR-TRIOXIDE BADI 67VCF
10/27/69
SULFUR-TRIOXIDE
PAGE 109
BURKDRfcSRST
CATHJ 45ST
CHFM
65ARF
CONVERTING SULFUR-DIOXIDE TO SULFUR-TRIOXIDE BAERE 26CSD
ABSORPTION OF SULFUR-TRIOXIDE IN A FOAM TYPE APPARATUS
HAVING AN INTERNAL FILM HEAT TRANSFER DEVICE
BLVAI A66AST
SULFUR-TRIOXIDE PRODUCTION WITH OXYGEN BY THE CONTACT METHOD
BOREGKA7STP
CATALYSIS OF SUL FUR-UIOX IDE TO SULFUR-TRIOXIDE BY METALS AND
PLATINUM-GOLD ALLOYS BORFGK53COS
CATALYSIS OF THE CONVERSION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE «Y METALS AND PLATINUM GOLD ALLOYS
BOPEGK53COT
THE DESIGN OF A UNIT FOR THE SYNTHFSIS OF SULFUR-TPIOX IOF.
HPUSH A60DA
HEMOVING SULFUR-TRIOXIOE FROM GAS MIXTURES
SULFUR-TRIOXIDE
PRODUCTION (IF SULFUR-TRIOXIOE
AMMONIA RECOVERY FROM WASHINGS OBTAINED DURING THE
PURIFICATION OF SULFUR-DIOXIDE AND SULFUR-TRIOXIDE
CONTAINING GASES CHEM
SULFUR-TRIOXIOE .FROM SULFUR-DIOXIDE CLARCB25STF
CATALYSTS FOR OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIOXIDE
DAVIP 59CFO
SULFUR-TRIOXIDE DAVIP 63ST
INFLUENCE OF CARBON-MONOXIDE ON THE ACTIVITY OF PLATINUM
CATALYSTS DURING THE OXIDATION PF SULFUR-DIOXIDE TO
SULFUR-TRIOXIOE EREMVV39IOC
AERODYNAMIC MODELLING OF CONTACT APPARATUS MODELLING OF A
REACTOR FOR THE OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE EP1AA &8AMO
SULFUR-TRIOXIDE PROCESS FARB 6«STP
DETERMINATION OF THE RATE OF CONVERSION OF SULFUR-DIOXIDE
INTO SULFUR-TRIOXIDE FIALGM6000T
STABILIZING LIQUID SULFUR-TRIOXIDE WITH PHOSPHORUS
CONTAINING COMPOUNDS f,ILREE64SLT
THE CONTACT OXIDATION OF SULFUR-DIOXIDE TP SULFUR-TRIOXIOE
UNDER PRESSURE GISTAM37TCO
MASS SPECTROHETRY OF MATERIALS PRODUCING SULFUR-TRIflXI OE
GOHLRS66MSH
STABILIZING SULFUR-TRIOXIOE GOLOT 64SST
CATALYTIC OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TO I OXIDE
FACTORS AFFECTING THE FORMATION OF SULFUR-TR IOX I Of INHUME
GASES HHDLAB67FAT
PURIFICATION OF SULFUR-DIOXIDE-BEARING GASES AND MANUFACTURE
OF SltLFUR-TRinXIDE HEIMAA32POS
CATALYTIC APPARATUS SUITABLE FOR CONVERSION OF
SULFUR-DIOXIDE TO SULFUR-TR IOXI OF ISENH02SCAS
MATHEMATICAL DESCRIPTION OF THE OXIDATION PF SULFUR-DIOXIDE
INTO SULFUR-TRinXIDE DURING WF T CATALYSIS KARTMBC>6MOn
SULFUR-TRIOXIDF KUHL 33ST
THE CATALYTIC PROPERTIES OF NONPLATINUM CATALYSTS IN THE
OXIDATION OF SULFUR-OinXIDE TO SULFUR-TR IOXI HE THE
ACTIVITY OF IRON-COPPER CATALYSTS
KIIRINP*OTCP
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SULFUR-TRIOXIDE
PAGE IK
SULFURIC-ACID
FORMATION OF SULFUR-TRIOXIDE APPLICATION OF INFRARED
SPECTROMETRY TO FUNDAMENTAL STUDIES LADNHP63FRT
CONTACT OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIOXIOE UNDER
PRESSURE LUKYPM33COO
FORMATION OF SULFUR-TRIOXIDE UNDFR THE ACTION OF ALPHA
PARTICLCS.. _ ___MAISJE27FOS
PRODUCT
OF SULFUR-TR I OX IDE BY THE CONTACT PROCESS
66POS
6SSTO
52ST
65POA
OX IDE
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META 52POS
CARBON-TYPE CATALYST FOR THE CONVERSION OF SULFUR-DIOXIDE
TO SULFUR-TRIOXIDE META 64CTC
MANUFACTURE OF SULFUR-TR IPX IDF. «ETA 64MOS
SULFUR-TRIOXIDE PROM GAS LOW IN SULFUR-DI flXIUE CONTENT
MFTA 64STF
THERMALLY BALANCED CATALYTIC OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE AND SULFURIC-ACID META 65TBC
PRODUCTION OF SULFUR-TRIOX IDE AND SULFUR IC-ACI D
META
SULFUR-TRIOXIOE OF SULFURIC-ACIO MFTT
SULFUR-TRIOXIDE NATI
PRODUCTION OF A GAS OF HIGH SULF UR-TRI OXIOt CONTENT
"ROD
PLATINUM-PALLADIUM CATALYST FOP. OXIDATION OF SULFUO-D
TO SULFUR-TRIOXIDE IOSE
DETERMINATION OF THE SPFf.P OF CONVERSION OF SULFUR-DIOXIDE
TO SULFUR-TRIOXIDE ON PASSING THROUGH A CATALYTIC LATTICE
SANSJ 360.SC
CALCULATION OF THE SULFUC- Tfl IOKI OE CATALYSIS SCHW 5ZCOT
CATALYTIC PROOUCTION OF SULFUR-TRIOXI DE SELD 77CPO
NOMOGRAMS FOR CALCULATING THE PERCENTAGE OF SULFUR-OI OX 1 DE
CONVERTED INTO SULFUR-TP IQXIDE AND THE COMPOSITION OF
OLEUM SHPASS36NCP
EFFECT OF CARRIERS ON THC ACTIVITIES AND PROPERTIES OF
VANADIUM CATALYSTS FOR THE OXIDATION OF SULFUR-TRIOXIOE
SOLCBI&4EOC
REACTION OF CALCIUM-CHLORIDE WITH SULFUR- TRIOXI UE
SUGIK F.6RCC
NEW CATALYST FOR THE RECOVERY I?F GASEOUS SULFUR COMPOUNDS
ANO THEIR TRANSFORMATIONS INTO SULFUR-TRIOXIDE
TERMR 64NCF
SULFURIC-ACID FROM SULFUR-TR IOXI OF VEVEV S4SAF
SULFUR-TRIOXIOE PROCESSING WESTNG67STP
SULFUR-TRIP GASES
FRUM CONTACT SULFURIC-ACID INSTALLATION CHCM 65UOS
CATALYTIC PROCESS FOR THE MANUFACTURE OF SULFUR IC-At10 IN
SEVERAL CONTACT AND ABSORPTION STEPS CMC" S6CPF
PREPARATION OF SULFURIC-ACID CHF." 66POS
SOME PROBLEMS CONCERNING SULFURIC-ACIO PRODUCTION
CIGDM 64SPC
PRODUCTION OF SULFURIC-ACIO BY THE CONTACT PROCESS
CIMAJ 67POS
DETERMINATION OF THE DEGREE OF OXIDATION HF SULFUR-DIOXIDE
IN THE MANUFACTURE OF SULFUR 1C-AC ID DEGO 5600T
PRODUCTION OF SULFUR IC-AC ID FROM FLUE-GAS FRI1.M nil TRFATMENT
OEG1 ICSftPOS
MANUFACTURING UP TO >.n PKR CFNT OLF.U" OR SULFURIC-ACID
DFRKJ <-<.TUT
PREPARATION OF VANADIUM-BASE CATALYSTS FOR THE SULFIJH 1C-AC ID
INDUSTRY DIACV SSPOV
SULFURIC-ACID PRODUCTION FROM f)PC ROASTER GASFS
DONnjRC>7SAP
ECONOMICS OF THF PRODUCTION OF SlILF UP IC-AC.! 0 FRO" WASTF
SULFUR CONTAINING G4SFS Fr-nPN"frSFnT
ALKALINE REITERATION OF VANADIUM FROM SCFVT r\T'.i.Yris <-"-w
SULFUR 1C-AC 11) PRODUCT"1 r.'ii HNA<.SAur
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10/27/69
SULFURIC-AC1D
PAGE 11?
CATALYST FOR SULFURIC-ACID PREPARATION
SULFUR 1C-AC ID
THE CHOICE OF RAW MATERIALS FO"
HAMPG 64CSA
HAHPG 64SAB
THE MANUFACTURE OF
HEIDH 67TCO
AND SULFUR-DIOXIDE ON THE
SULFURIC-ACID
EFFECT OF HYDROGEN-SULFIDE _..
CORROSION OF CHEMICALLY RESISTANT CHROMIUM NICKEL STEEL
-•• ' -•" — WITH SULFURIC-ACIO
IN A SODIIIM-SULFATE SOLUTION ACIDIFIED
HERBG 66EHS
SULFURIC-ACID OPTIMIZED CONDITION IN CONTACT MANUFACTURE
HOMMAC61SAO
AN AUTOMATIC CONTROL SYSTEM FOR THE DRYING AND ABSORPTION
CYCLE IN SULFURIC-ACIO PRODUCTION IGRFV 67ACS
SULFURIC-ACIO JAEGA027SA
THE DOUBLE CONTACT PROCESS OF SULFURIC-ACID MANUFACTURE
KAMIY 67DCP
THE EFFECT OF HIGH CONCENTRATIONS OF SULFURIC-ACID ON THE
RATE OF OXIDATION OF SULFUR-DIOXIDE IN THE PRESENCF OF
BIVALENT MANGANESE IONS
SPECTROGRAPHIC AND X-RAY DIFFRACTION STUDY OF
CATALYST FOR SULFURIC-ACID MANUFACTURE
REMOVAL OF SULFUR-DIOXIDE FROM STACK GASES
SULFURIC-ACID PLANTS
VANADIUM CATALYTIC MASSES IN MANUFACTURE OF
OF
KASHLI36TEO
IRON-OXIDE
KOZHNV66PAX
KPISSR66RSD
SULFURIC-ACID
KRUME 41VCM
OXIDATION OF SULFUR-DIOXIDE BY NITROSE IN SULFURIC-ACID
KUNI H4600S
PRODUCTION OF SULFURIC-ACIO KUZHIN64POS
REMOVAL OF NITROGEN-OXIDE CONTAINING SULFURIC-ACIO FUMES
LAMMC 66RNO
SULFURIC-ACIO BY CONTACT PROCESS LAMMC 66SAC
FFFECT OF FUEL CHARACTERISTICS AND EXCESS COMBUSTION AIR
ON SULFURIC-ACID FORMATION IN A PULVERIZED COAL-FIRED
BOILER LEE GK67EFC
INFLUENCE OF REACTION RATE ON OPERATING CONDITIONS IN THE
CONTACT SULFURIC-ACIO MANUFACTURE LEWIWK25IOR
NOTE ON THE INFLUENCE OF REACTION RATE ON OPERATING
CONDITIONS IN SULFURIC-ACID MANUFACTURE LEWIWK26NOT
CONVERSION STAGE IN THE MANUFACTURE OF SULFURIC-ACIO BY
CONTACT PROCESS LCWRGC58CSI
DEVELOPMENT OF CONCEPTS ON REACTION MECHANISM OF
SULFURIC-ACID PRODUCT ION MALIIK6600C
SULFURIC-ACID CONCENTRATION PROCESS MANTR 67SAC
PURIFICATION OF SULFUPIC-ACID IRON CONTAINING WASHING
DISCHARGES MATAVL67PSA
SELECTION OF CAST IRONS RESISTANT TO CORROSION BY
CONCENTRATED SULFURIC-ACIO MAZAK 66SCI
SULFURIC-ACID FROM SULFUR-DIOXIDE CONTAINING GASFS
META 64SAS
THERMALLY BALANCED CATALYTIC flXIdnTION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIOE AND SULFURIC-ACin 1ETA 65TRC
HEATING AND COOLING OF SULFUR IC-AC ID CONTACT CONVERTERS
MFTA 66HAC
PRODUCTION OF SULFURIC-ACIn MFTT 65PSA
10/27/69
SULFURIC-ACID
SULFUH-TRinxIDE OF SULFURIC-ACID
S03_AND SyL.FURJ.C-AC ID BY CATALYTIC CONVERSION OF GASES
"TA " """" •"•-
PAGE 113
HETT 65STO
CONTAINING S02
PRODUCTION OF SULFURIC-ACIO
PREPARING SULFURIC-ACID BY THE NITROSE METHOD
A SIMPLIFIED PREPARATION FOR SULFURIC-ACID
SPRAY COOLER TUBES IN SULFURIC-ACID MANUFACTURE
PREPARATION OF SULFURIC-ACID RY NITROSE METHOD
66SAS
METTAL65PSA
MIKHK 67PSA
MONT 65ASP
MORAAM66SCT
MOROBI67POS
THE USE OF CONTACT EQUIPMENT WITH A FLUIDIZED CATALYST BED
IN THE MANUFACTURING OF SULFURIC-ACID MUKHIP63TUO
PRODUCTION OF TOWER SULFURIC-ACID RY A PROCEDURE INVOLVING
ACID CIRCULATION WITH A CROSS-OVER CYCLE NEIPKV64POT
THE REACTION MECHANISM IN THE CONTACT SULFURIC-ACID PROCESS
AND THE METHOD OF ACTION OF ACTIVATORS NEUM8 29TRM
SULFURIC-ACIO CATALYSIS WITH IRON-OXIDE NEUMB 37SAC
VANADIUM CATALYSTS FOR THE PRODUCTION OF SULFURIC-ACID
OKAMT 60VCF
THE MANUFACTURE OF SULFURIC-ACID BY MEANS OF VANADIUM
CATALYST ON AN INTERMEDIATE SCALE II. INCREASE OF THE
DRAFT RESISTANCE IN A SMALL CONVERTER OSAffG 39TMO
MANUFACTURE OF SULFURIC-ACID BY VANADIUM CATALYST III
INCREASE OF THE DRAFT RESISTANCE IN THE LARGE CONVERTER
OSAMG 43MOS
SULFURIC-ACID PAULFM66SA
CORROSION OF LEAD ALLOYS IN SULFURIC-ACID PELZVE67CLA
USE OF GRAPHITE BLOCKS FOR PROTECTION OF SCRUBBING TOWERS
IN THE SULFURIC-ACID PLANT OF UST-KAMENOGORSK LEAD-ZINC
COMBINE PEREYP67UGB
REMOVAL OF SULFURIC-ACID FOG FROM GASES PETEFH62RSA
CONTROL FLOW-SHEETS IN THE OPERATION OF SULFURIC-ACID
CONTACT INFORMATION PETRNM66CFS
PRODUCTION OF SULFURIC-ACIO POZIME64POS
PRODUCTION OF OLEUM IN THE MANUFACTURE OF SULFURIC-ACIO BY
THE SHORTENED CONTACT PROCESS REZIIG6SPOM
CONTROLLING CORROSION IN WET-GAS SULFURIC-ACID PLANTS
RINCJB67CCU
SULFURIC-ACID MANUFACTURE RINCJB67SAM
SULFURIC-ACID ROBSS 25SA
PRODUCTION OF SULFURIC-ACIO RUGHAL65POS
KINETICS OF THE CATALYTIC FORMATION OF SULFURIC-ACID ON A
BARIUM-ALUMINUM-VANADIUM CATALYSTS RZAEPB60KOT
EFFECT OF SULFURIC-ACIO CONCENTRATION ON REGENERATION OF
NITROGEN-OXIDES IN A TOWER SYSTEM SAVIEI66EOS
EFFECT OF IONIZING RADIATIONS ON THE SULFUR-DIOXIDE-OXYGEN
SYSTEM II THE OXIDATION OF SULFUROUS-AC10 TO SULFURIC-ACID
BY ACTION OF X-RAY RADIATION SCHRR 64EOI
SULFURIC-ACID PRODUCTION PROCESSING TECHNIQUE DEVELOPMENT
SEFEB f>TSAP
SULFURIC-ACID PRODUCTION WITHOUT COLUMN PACKING
SHEVDM64SAP
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10/27/69
SULFURIC-ACID
PAGE
COMBINATION CONTACT-TOWER PROCESS FOR SULFURIC-ACID
MANUFACTURE SMYSNI67CCT
SULFURIC-ACID SOC. 27SA
DETERMINATION OF THE DEGREE OF OXIDATION OF SULFUR-DIOXIDE
IN THE MANUFACTURE OF SULFURIC-ACID SDCIET56DDO
ELECTROSTATIC DEPOSITION OF SULFURIC-ACID MISTS FROM THE .
WASTE GASES OF SULFUR 1C-ACI0 MANUFACTURE STOPK 65EOS
ELECTROCHEMICAL METHOD OF PRODUCTION OF SULFURIC-ACID
OPTIMUM COMPOSITION OF NITROSE IN SULFURIC-ACI0 PRODUCTION
BY THE MILLS-PACKARD-PROCESS TSEIAN660CO
REASONS FOR THE RISE IN THE TEMPERATURE OF GASES IN FRONT
OF THE CONTACT APPARATUS OF AN INSTALLATION FOR PREPARING
SULFURIC-ACID BY WET CATALYSIS METHOD TSYGSA67RFT
SULFURICrACID AND FERTILIZERS . VAHETK67SAA
ELECTROLYTIC PRODUCTION OF SULFURIC-ACID VASISV50EPO
SULFURfC-ACID FROM SULFUft-TftinxiDE VEVEV 64SAF
CATALYTIC CONVERSION OF SULFUR-DIOXIDE INTO SULFURIC-ACI0
SULFURIC-ACID
SULFURIC-ACIO RECOVERY FROM COKE OVEN OFF-GAS
VORTG 19CCO
WALTJH40SA
ILBDE68ROI
WUNDG 64SAR
REDUCING DISCHARGE .INTO THE ATMOSPHERE OF SULFURIC-ACID MIST
MINIMIZING SULFURIC-ACID VAPOR DISCHARGE INTO THE
ATMOSPHERE ZII
SULFURIC-ANHYORIDE
MAKING SULFUR 1C-ANHYDRIDE ELLIC 17MSA
DELETERIOUS ACTION OF RHODIUM AND OF IRIDIUM UPON PLATINUM
IN THE CATALYSIS OF SULFURIC-ANHYORIDE LEVIGR27DAO
TREATMENT OF GAS FOR SULFURIC-ANHYORIDE MANUFACTURE
MERRHF27TOG
CXIOE
GLASS-WOOL FILTERS FOR TRAPPING SULFURIC-OXIDE MIST
YASHEV65GHF
SULFURI C-l
SULFUROUS
PURIFICATION OF SULFUROUS RESIDUAL GASES BY ALUMINA BED
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PROCESS FOR EXTRACTION OF VALUABLE PRODUCTS FROM SCHISTS
AND OTHER BITUMINOUS FERRUNGINOUS AND SULFUROUS SEDIMENTS
AND COMPOUNDS MANUFACTURED THEREFROM LUPAK 66PEV
CATALYTIC PROPERTY OF VANADIUM-OXIDE IN THE REDUCTION OF
SULFUROUS GAS BY CARBON-MONOXIDE VISCYS45CPQ
SULFUROUS-ANHY OR IOE
ENTROPY OF THE ACTIVE COMPLEX IN THE OXIDATION OF
SULFUROUS-ANHYORIOE OVER PT CATALYST GOLOGIASEOT
THE INFLUENCE OF THE CARRIER ON THE ACTIVITY OF THE VANADIUM
CATALYSTS FOR THE OXIDATION OF SULFUROUS-ANHYORIOE
SOLOBI64TIO
STUDY OF THE OXIDATION OF SULFURDUS-ANHYDRIDE AND AMMONIA
GAS IN THE PRESENCE OF PLATINUM AND RHODIUM
WENC.P 1BSOT
SUPPORT
GRADED SUPPORT BED FOR CATALYSTS
CHRICMftSGSB
10/27/69
SUPPORT
SUPPORTED
NUPPOPTS
SURFACE
CATALYST SUPPORT MEANS
POROUS SUPPORT FOR FLUIniZED-RED CATALYSTS
PAGE 115
MOMS 65CSM
SELIHJ67PSF
SUPPORTED PLATINUM METAL CATALYSTS
«CTHODS OF USE IN INDUSTRIAL PROCESSES
THEIR SELECTION AND
BOIYDGC65SP*
CONNJF67RSP
HAUEAP6SOMG
KIIEZW ft2CCS
EXAMINATION
MOSSRL67SSP
SINFJW.7CSM
KFCRYSTALL IZATION OF SUPPORTEI1 PLATINUM
CATALYTIC ACTIVITY OF SIIPPORTEO PLATINUM
riPEN MESH GLASS-FABRIC SUPPORTED CATALYST
CHROMIC CATALYSTS SUPPORTfn ON AL213
THE ST-UJCrilRF OF SU'PQRTm PLATINU" CATALYSTS
BY ELECTRON MICRC.'SC"Pv
CATALYSIS OVER SUPoORTtP KfTALS _. .......,,
SCWPTI1N PRQPFPTICS OF SUPPORTED POTASSIIIM-VANAOATE CATALYST
SZEKG 66SPO
CATALYTIC SUPPORTS DUFFF &7CS
CATALYST SUPPORTS MOMS 21CS
DEPOSITING METALS ON SILICEOUS CATALYST SUPPORTS FPOM AMINE
COMPLEXES IN AQUEOUS AMMONIA SOLUTIONS MULABF670MS
CATALYST SUPPORTS PAPCO 66CS
POWDERED METAL REACTION AGFNTS PARTIALLY E"BEOnED IN MFTAL
SUPPORTS SAES 6ftPMP
CATALYST SUPPORTS SOC I f-ftCS
SYNTHETIC ZEOLITES OFFE" UNIOUF PROPfcRTIES AS CATALYST
SUPPORTS STPRDH64SZO
CATALYSTS SUPPORTS VFRE 35CS
INVESTIGATIONS OF POROUS ADSORBENTS AND CATALYSTS BY MEANS
OF DISTRIBUTIVE FUNCTIONS OF THE SIIRFACF Wl TK REGARD TO
ITS CURVATURE HUKUl 661 PA
MECHANISM OF OXIDATION HVDROGENAI ION AND ELFCT Rnr.HF«MC AL
COMBUSTION ON SOLID CATALYSTS CATALYTIC PFCULIARITIFS
OF SURFACE OXIDES ON CARBON OAVTOKMMOH
HYDRODYNAMICS AND "ASS TRANSFER IN A NOZZLELESS VENTUP.I
ABSORBER ADSORPTION OF SULFUR-DIOXIDE INTO WATEK
AND WATER SOLUTIONS OF SURFACE ACTIVE AGENTS
F.LEND 66HMT
THE INFLUENCE OF SURFACE COVERAGE ON CATALYTIC EFFECTIVENESS
AND SELECTIVITY THF ISOTHFRMAL AND NONISOTHERMAL CASES
HUTCJ 6
THE VARIATION WITH TE^PfiRATURF r?F THE CATALYTIC ACTIVITY
OF AN OXIDIZED STAINLESS STFEL SURFACE IN THC OXIDATION
SF SULFUR-DIOXIDE JACKPJS9VTC
FACE STRUCTURE OF KIESELGUHR CARRIERS AND CATALYSTS FOR
THE OXIDATION OF SULFUR-DIOXIDE JIRUP 57SSO
OVERALL CATALYTIC EFFFCTIVENESS FACTORS AND THEIR SHAPE
CORRELATIONS WITH MASS TRANSFER AND REACTION ON THF
EXTERNAL SURFACE KASAS f.7OCE
CATALYST AND FNZYME THE PROBLEM or SURFACE ACTIVITY OF
NATURAL SUBSTANCES KRBnN!*?CAF
EFFECT OF THE EXTERNAL SURF-ACE ON THE REACTION RATE AND
SELECTIVITY OF I SflTHFOMAl. CATALYST PARTICLES
KHAU'. !/.«,: I""
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10/27/69
SURFACE
SURFACES
T-S/R
TANTALUM
TEMPERATURE
EFFECTIVENESS FACTORS WITH SURFACE DIFFUSION
EFFECTIVENESS FACTORS WITH SURFACE DIFFUSION
THE DETECTION OF PREMATURE GRADUAL CHANGES OF THE SURFACE
PAGE 116
KRASJH55EFW
KR4SJH65EFS
LAYER OF SOLID BODIES AS ILLUSTRATED BY V205
KRAUA 64TDO
ORIGIN OF THE COMPENSATION EFFECT IN CHEMICAL REACTIONS
OCCUR ING ON THE SURFACE OF SEMICONDUCTOR CATALYSTS
KUZNVS6M30T
PROBLEMS IN THE SURFACE CHEMISTRY OF METALS NAGAS 66PIT
CATALYTIC OXIDATION OF SULFUR-DIOXIDE BY HEAVY HYDROGEN
ON THE SURFACE OF A PLATINUM SPONGE NAKAS MCOH
SURFACE MODELS IN HETEROGENEOUS CATALYSIS PARRG 66SMI
CATIONIC SCREENING AND SURFACE REACTION PHENOMENA
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FLOW OF SULFUR-DIOXIDE OVER THF SURFACE OF SPHERON-6(2700)
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SURFACE BY THE ELECTROCHEMICAL METHOD IN OXYGEN
CHEMISORPTION SIEDJ 6SDNA
COMPARATIVE CATALYTIC ACTIVITY OF CENTERS ON THE SURFACE OF
CRYSTALS AND OF AN INERT CARRIER STREZV64CCA
EFFECTS OF THE DISTRIBUTION OF PORE LENGTHS IN CATALYST
PARTICLES ON THE CATALYST EFFICIENCY IN AN IRREVERSIBLE
SURFACE REACTION OF THE FIRST ORDER TARTR 66EDP
METHODS OF INVESTIGATING THE SURFACE PROPERTIES OF CATALYSTS
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THE T-S/R AND I-S/R DIAGRAMS FOR IOEAL-GASFS
FISCS 66TTS
ACTION OF SULFUR-DIOXIDE ON TITANIUM ZIRCONIUM HAFNIUM
VANADIUM NIOBIUM AND TANTALUM OAV1L 6?ASD
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THE IGNITION TEMPERATURE OF A WEAR RFSISTANT VANADIUM
CATALYST FOR THE OXIDATION OF SULFUR-HI OXIDE
CHERMAfrSTIT
10/27/69
TEMPERATURE
TEMPERATURES
PAGE 117
_ _ . . _ DAMKG A3ETI
. OF TEMPERATURE ON THE RATE OF FORMATION OF SULFURIC
BY THE OXIDATION OF SULFUR-DIOXIDE ON ACTIVATED CARBON BY
EXCESS TEMPERATURE IN CATALYST GRAINS
EFFECT OF TEMPERATURE ON THE RATE OF F_
-::-;:. . SULFUR-DIOXIDE ON ACTI
THE LIQUID CONTACT METHOD DAVTOK61ETR
CONTROL OF TEMPERATURE BY ADMISSION OF A COLO COMPONENT AS A
MEANS FOR ENSURING OPTIMAL CONDITIONS FOR AN EXOTHERMIC
REACTION
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ALLOWANCE FOR THE TEMPERATURE DEPENDENCE OF SPECIFIC HFAT
OF INDIVIDUAL GASES AND GAS MIXTURES IN THERMODYNAMIC
CALCULATION FOR GAS FLOW MACHINE FISCS 65ATD
TEMPERATURE RELATION FOR THE RATE OF OXIDATION OF
SULFUR-DIOXIDE ON VANADIUM CATALYSTS GEIBEV56TRF
SEARCH FOP CATALYSTS FOR THE OXIDATION OF SULFUR-DIOXIDE
WITH A DECREASED IGNITION TEMPERATURE GERBEV63SFC
THE VARIATION WITH TEMPERATURE OF THE CATALYTIC ACTIVITY
OF AN OXIDIZED STAINLESS STEFL SURFACE IN THE OXIDATION
OF SULFUR-DIOXIDE JACKPJ59VTC
INFLUENCE OF TEMPERATURE ON THF OXIDATION OF SULFUR-DIOXIDE
WITH OXYGEN IN THF PRESENCE OF CATALYSTS AND CATALYST
POISONS KASHLI35IOT
REACTOR FOR CATALYTIC EXOTHERMIC REACTIONS AT ELEVATED
TEMPERATURE KAUTO 66RCE
USE OF THERMODYNAMIC SIMILARITY FOR THE DETERMINATION OF
BOYLE-CURVES OF SUBSTANCES STUDIED IN A LIMITED
TEMPERATURE INTERVAL KAZAYZ66UTS
TEMPERATURE AND CONCENTRATION DISTRIBUTION IN A PACKED-BED
REACTOR OKI Y f>6TAC
EFFECT OF CONCENTRATION GRADIENTS OF REAGENTS AND THE
TEMPERATURE ON THE EFFICIENCY OF POROUS CATALYST PARTICLES
AND THE LIMITS OF EXISTENCE OF STEADY STATE CONDITIONS
PISMLM66EOC
THE MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE INFLUENCE OF TEMPERATURE AND TIME OF CARRON
DESORPTION ON ADSORPTION AND OXIDATION OF H2S AND S02
SIEDJ 64MCO
OXIDATION
COMPUTATION OF THE ADIABATIC TEMPERATURE FOR THE .._.
OF SULFUR-DIOXIDE SIMEA 66CHT
APPARATUS FOR TEMPERATURE CONTROL IN CATALYTIC REACTIONS
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EFFECT OF HIGH TEMPERATURE PLASTIC DEFORMATION AND
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PROPERTIES OF CHROMIUM NICKEL AUSTENTIC STEELS
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ANALYTICAL PREDICTION OF CONCENTRATION AND TEMPERATURE
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REASONS FOR THE RISE IN THE TEMPERATURE OF GASES IN FRONT
OF THE CONTACT APPARATUS OF AN INSTALLATION FOR PREPARING
SyLFyRIC-ACID_RY_WFT CATALYSIS METHOD __ .....-TS YGSA67RFT
THERMOGRAPHIC DETERMINATION
VANADIUM CATALYSTS
MAXIMUM TEMPERATURE INSIDE A POROUS CATALYST
THE IGNITION TEMPERATURE FOR
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SEMIFACTORY SCALE STUDIES OF VANADIUM CATALYSTS WHICH ACT AT
LOW TEMPERATURES QRCIDK I 34SSS
152
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C4TAIYSTS IN THE IMITATION Of- SHI FIJP -Dl OX IDE AT LOW
TEMft-'fAT'lKFS GCP6EV63FQP
THERMAL CONDUCTIVITY OF SULFUH-DIOXIOF AND DIFTHYL-ETHFP
AT DIFFERENT TEMPERATURES GUPTA067TCS
THE IGNITION TEMTERATURFS OF VANADIUM CATALYSTS
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OF AN ?yI^ATI0^4 C.A1AI.VSTS FOR USE AT HIGH
S ROSS 67MOA
GAS CATALYSIS AT HIGH TFMPFPATUKES
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UET"M|Nnr, THE KETARfiAT lO.V DFGREE OF THF THERMAL
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THE"M4L RADIATION ANO CHEMICAL STABILITY OF SUL.F IIR-Df OX I HE
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THERMAL EFFECT IN CATALYTIC OXIDATION OF SULFUR-DIOXIDE
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CONTROL OF AIR POLLUTION FROM LARGE THERMAL POWER STATIONS
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THERMAL CONDUCTIVITY OF SULFUR-DIOXIDE ANO DIETHYL-ETHER
AT DIFFERENT TFMPFR ATIIRES GUPTAD67TCS
Ki!S!M>", THE THERMAL RESISTIVITY OF THE V705 CATALYST BY
ALUMINUM-HYDROXIDE KRAIIA 62RTT
ATTEMPTS TO INCREASE THE THERMAL RESISTANCE OF THE
INDUSTRIAL VANADIUM CATALYST IN THE REACTION OF OXIDATION
OF S02 KUCZW 50ATI
COMPARATIVE RESULTS FOR THERMAL AND ELECTRONIC ACTIVATION OF
MIXTURES OF SiJLFUR-OinxiOE AND OXYGEN MPYEAJftSCRF
APPARATUS FOR INDICATING THE THERMAL EMF AND AC
CONDUCTIVITY OF A CATALYST R1CHJT66AIT
THERMAL-CONDUCT IVITY
THERMAL-CONDUCTIVITY UF BINARY MIXTURES OF SULFUR-DIOXIDE
AND INEPT GASES GUPTADfcTTCB
PAGE 119
THERMALLY
THERMO
THERMODYNAMIC
ACTIVITY OF THERMALLY STABLE VANAOIUM CATALYSTS FOB THE
OXIDATION OF SULFUR-HIPXIDE KUNITIMAflT
THERMALLY BALANCED CATALYTIC OXIDATION OF SULFUR-Dl OXIDF TO
SULF'.IR-TRIOXIDF AND SUl FURIC-AC ID
THERMO PROPERTIES OF NON-HYDROCARBONS
PROPERTIES OF SULFUR-DIOXIDE
META
THERMOOYAMIC
CANJLN66TPN
ALLOWANCE FOR THE TEMPERATURF DEPENDENCE OF SPECIFIC HEAT
OF INDIVIDUAL GASES anO GAS MIXTURES IN THERMQDYNAMIC
CALCULATION FOR r,A S FLt'W MACHINE FISCS
THERMHOYNA-IC CONSIDERATION OF CATALYTIC OXIDATION
KATOA
USE OF THER*OOYNA«MC S|MIIA»|IY KP» 1HE OH TERMI NATION OF
POYLE-CURVES OF SU^STANCFS SMIIlICn IN A LIMITED
TEMPERATURE INTERVAL
KAZAY.'.ft6UTS
THF.RMODYNAMIC
THERMODYNAMICS
THERMOGRAPHIC
TIME
TIME-DEPENDANT
i IN
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TOMBAC
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THERHOOVNAMIC CONSIDERATION ON THF CATALYTIC OXIDATION OF
CARBON-MONOXIDE AND SULFUR-DIOXIDE SEIYT 61TCO
APPLIED HYDROCARBON THEPMOOYNAMICS HEAT CAPACITY OIFFERFNCES
EDMIWCA7AHH
APPLIED HYDROCARBON THERMODYNAMICS IDEAL GAS STATE
PROPERTIES EDMIUCf-TAHT
THERMOGRAPH 1C STUDY OF TH6 CATALYTIC OXIDATION OF
SULFUP-OIOX IDE ON VANADIUM-OXIDE SATAV 59TSC1
STUDY OF CORROSION OF IRON AND ITS ALLOYS IN CHLORINE AND
SULFUR-DIOXIDE BY THE THERMOGRAPHIC METHOD TOVMIK66SCI
THERMOGRAPHIC DETERMINATION OF THE IGNITION TEMPERATURE FOR
VANADIUM CATALYSTS VI SHI V63TDO
THE MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE INFLUENCE OF TE«»E<»ATURE »ND TIME OF CARBON
DESORPTION ON ADSORPTION AND OXIDATION OF H?S AND SO?
SIEDJ 64MCO
CATALYTIC OXIDATION OF SULFUR-DIOXIDE AS A FUNCTION OF
RESIDENCE TIME OF THE GASES IN THE REACTION CHAMBER
WICKK 61C00
TIME-DEPENDANT PORE-MOUTH POISONING OF CATALYSTS
CARBJJ66TDP
THE EFFECT OF METAL OXIDE ADMIXTURES ON THE ACTIVITY OF THE
TIN CHROMIUM CATALYST GFRNDV35TED
ACTION OF SULFUR-DIOXIDE ON TITANIUM ZIRCONIUM HAFNIUM
VANADIUM NIOBIUM AND TANTALUM OAVIL A2ASO
BEHAVIOR OF TOMBAC ALLOY IN SOME CORROSIVE MEDIA
MERMS &ABTA
ABSORPTION OF SULFUR-TRIOXIDE IN A FOAM TYPE APPARATUS
HAVING AN INTERNAL FILM HEAT TRANSFER DEVICE
BLYAIG68AST
MASS TRANSFER CDEFFICIEMTS DURING THE ABSORPTION OF S02
FROM GASES BY AMMON IU«-SULF I TE-BI SULF I TE SOLUTIONS
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HEAT TRANSFER ANALOGY FP9 DIFFUSION AND FIRST OROEP CHEMICAL
REACTION IN A CATALYST
MATHEMATICAL MQUELS OF CATALYTIC RF.ACTORS
TRANSFER
HYDRODYNAMICS AND MASS TRANSFER IN A NOZZLELESS VENTURI
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HEAT AND MASS
CYBUA 67MMO
AND MATER SOLUTIONS OF SURFACE
AGENTS
IMPROVEMENT OF THE MASS TRANSFER F»OM A GAS TO A
CATALYST OR ADSORBENT BY PRESSURE OSCILLATIONS
HEAT AND MASS TRANSFER IN CATALYTIC BEDS
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'PFATMENT-X
PAGE I2r
MDDEl L INT, HF CHEMICAL REACTORS HEAT AND MASS TRANSFER WITHIN
A POPn'JS CATALYST "ARTICLE SOME RESULTS OF AN ANALYSIS
FOP A ZERO-ORDER REACTION HLAVV 67MOC
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS II. THE
EFFECT OF CATALYST CONDUCTIVITY ON THE APPARENT
CONDUCTIVITY OF THE CATALYST BED AND THE HEAT TRANSFER
COEFFICIENT FROM THE HFD TO REACTPR BATH HORAJ 67HAM
OVERALL CATALYTIC EFFECTIVENESS FACTORS AND THFIP SHAPE
CORRELATIONS WITH MASS TPANSFE" AND ^FACTION I'N THE
EXTERNAL SURFACE KASAS S70CE
MASS TRANSFER IN A SCRUBBER WITH CONE-SHAPFD GRID PLATES
K H OK S F 6 5 M T S
HEAT AND MASS TRANSFER FOR HETEROGFNEOUS CATALYSIS
KONDP 6RHMT
THE CHARGE TRANSFER THEORY OF GAS-SUPFACE INTERACTIONS AND
HETEROGENEOUS CATALYSIS ON SEMICONDUCTORS LEE VJ64TCT
HEAT TRANSFER IN GRANULAR REDS TEHPERATUR DISTRIBUTION
IN THE CATALYST BEOS FOR SULFUR-DIOXIDE OXIDATION
*^AFDS 5 1 HT I
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS VII EFFECT
"OF CATALYST HEAT CONDUCTIVITY ON THE OVFRALl. HEAT
TRANSFER COEFFICIENT IN A PACKED TUBE MAMUP 67HAM
MODELLING OF CHEMICAL REACTORS VI. HEAT AND MASS TRANSFER
IN A PnoQUS CATALYST "ARTICLE THF MULTIPLICITY OF SOLUTION
FOR THE CASE OF AN EXOTHERMIC ZFRO-PRDER REACTION
MAREM 6RMOC
MASS TRANSFER AND ABSORPTION WITH REACTION IN RPTAPY
TYPE FOUIPMFNT NIKON 6C.MTA
CALCULATION OF HFAT TRANSFER COEFFICIENTS IN TUBULAP
CATALYTIC RFACTORS SADOAS6SCOH
MASS AND HEAT TRANSFER IN GAS-SOLID SYSTEM WICKF S1MAH
MASS TRANSPORT AND CHE1ICAL REACTION IN MULTIFUNCTIONAL
CATALYST SYSTEMS DIINNDJfrSMTA
EFFECT OF TRANSPORT ON THF KINETICS OF OXinATION OF
SULFUR-DIOXIDE ON A UAH I UM-ALUMI NUM-VANAOIIJM CATALYST
INVESTIGATION BY THE OIAPHPAM «•<= THOD ROITVASBFOT
APPARATUS AND PROCHSS FHR CIPCULATING POWDERED S?l. Ill IN
CHFMIC.AL TRHATMENT-X HFMMCT57AAP
HFAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS VII FFFF-CT
OF CATALYST HEAT CONOUC T IVI T Y ON THE OVERALL H?AT
TRANSFER COEFFICIENT IN A PACKED TUP-E MAMUP 67HAM
HATE OF ABSORPTION OF SOLUBLE GASFS IN A Wf-TTFD HALL TUBE
ABSORPTION OF S03 BY SULfUP.IC-AC ID-MONOHYDRATE
RAMHVMS5RAS
ANALYTICAL P"FDICTION [IF CONCENTRATION AND TtMPFRATIJPE
PROFUFS IN A PACKED CATALYTIC TUBF TPNES
HETEROGENEOUS CATALYSIS USING A TUBE C.ATAIYST !. NSTIIRG OF
THF. MHTHOO YiiZKSLSSHr.
CATALYIIC OXIDATION TO SULFUP-TRIOXIW AND THE THEORY OF
RAPID CATALYTIC "ROCtSSES II. C.FNFRAL o.ULE FUR GAS
DIFFUSION TUBES EFFECT OF DILUTION WITH INPUT GASFS
AMI1PI
•155
10/27/69
TUBES
TUBULAR
TERRACED HEATFRS FOR CATALYSTS FILLED TUBES
SPRAY COOLER TUBES IN SULFURIC-AC ID MANUFACTURE
PAGE 121
LEE FA66THF
MORAAM66SCT
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BAROT 52RKI
ULTRA-VIOLET
ULTRASONIC
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VANAOIA-T ITANIA
TUBULAR HEAT EXCHANGER FOR THE CONTACT UNITS OF
SULFURIC-AC 10 PLANTS
REACTION KINETICS IN A T'lBULAR REACTOR
DESIGN OF FIXED-BED TUBULAR CATALYTIC REACTORS
CARPS 62DOF
STABLE AND UNSTABLE BEHAVIOR OF AD1ABATIC TUBULAR REACTOR
AS FOR EXAMPLE IN CATALYTIC CO OXIDATION PAOBG 67SAU
CALCULATION OF HEAT TRANSFER COEFFICIENTS IN TUBULAR
CATALYTIC REACTORS SADOAS65COH
STUDY OF THE CATALYTIC ACTION OF ULTRA-VIOLET RAYS
THE OXIDATION OF SULFUP-DIOXIDE IN ULTRA-VIOLET L?GH?L 22SflT
KORNG a^TOO
INFLUENCE OF THE ULTRASONIC FIELD ON THE CATALYTIC ACTIVITY
OF HN02 PREPARED BY ELECTROLYSIS KOWAE 65IUF
ACTION OF ULTRASONIC WAVES ON CHEMICAL AND PHYSICOCHEMIC 4L
PROCESSES LE BA 6TAUH
ULTRASONICALLY ACTIVATED CATALYSTS FOR CHEMICAL REACTION
JONEJB66UAC
VANADIUM
EFFECTS OF X-RAY IRRADIATION ON THE OXIDATION
SULFUR-DIOXIDE BY VANADI A-T I TANI A CATALYSTS
OF
KUBflT 57EOX
VANADIUM CATALYZERS FOR THE PRODUCTION OF SULFUR IC-AC ID
RECOVERY OF VANADIUM FROM THE CATALYST USED IN TH^CCNT ACT*"
ACID PROCESS ALREFMA4ROV
VANADIUM CATALYST FOR OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOX IDE BADI 62VCF
VANADIUM CATALYSTS BARTJ
VANADIUM CATALYZERS FOR SULFUR IC-AC ID PRODUCTION
MECHANISM OF OXIDATION OF SULFUR-DIOXIDE IN THE
OF ACTIVATED VANADIUM CATALYSTS INFLUENCE OF AN
ADMJXTURE OF SALTS OF ALKALI ELEMENTS AND AMORPHOUS
MECHANISM OF THE OXIDATION OF SULFUR-DIOXIDE IN THERPRESENCE
OF ACTIVATED VANADIUM CATALYSTS STABILITY OF VANADIUM
COMPOUNDS UNDER THE CONDITION OF SULFUR IC-AC I D CATALYSIS
THE KINETICS OF SULFUR-DIOXIDE OXIDATION OVER VANAO?UMK*°MOT
SEMIFACTORY SCALE STUDIES OF VANADIUM CATALYSTS WH?CHGACTT AT
LOW TEMPERATURES RRODKIS^SSS
PROMOTING ACTION OF GROUP- I AND THE LANTHANIDE -GROUP
ELEMENTS ON VANADIUM CATALYSTS BROOK Ift^P AC.
156
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10/27/69
VANADIUM
PAGE 1?2
VANADIUM CATALYSTS IN THE OXIDATION OF S02 BRUSH 66VCI
CONTAMINATION OF_A_VANADiyM CATALYST WITH CARBON-BLACK . I N_
SULFUR!
ID PRODUCTION
BURYKA63COA
CALCULATION OF THE RATE OF REACTION CONSTANTS IN THE
OXIDATION OF SO2 TO S03 ON A VANADIUM CATALYST
SURYKA63COT
-DIOXIDE
WITH A COMMERCIAL VANADIUM CATALYST A KINETIC STUDY
CALOPH52TMO
STUDIES OF THE RATE OF REACTION IN THE VANADIUM CONTACT
SULFURIC-ACID PROCESS CHANHY36SOT
KINETIC STUDIES ON THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYSTS III. A COMPARISON OF THE RATE EQUATIONS
OBTAINED WITH SOME INDUSTRIAL VANADIUM CATALYSTS
CHANMC59KSO
THE IGNITION TEMPERATURE OF A WEAR RESISTANT VANADIUM
CATALYST FOR THE OXIDATION OF SULFUR-DIOXIDE
CHERMA65TIT
ACTION OF SULFUR-DIOXIDE ON TITANIUM ZIRCONIUM HAFNIUM
VANADIUM NIOBIUM AND TANTALUM DAVIL 62ASD
THE EFFECT OF ALKALI METAL SULFATES ON THE CATALYTIC
PROPERTIES OF VANADIUM OZISAP61TEOi
THE RATE OF OXIDATION OF SULFUR-DIOXIDE WITH A COMMERCIAL !
VANADIUM CATALYST EKLURB57TRO I
ACTIVITY STRUCTURE AND ELECTRICAL PROPERTIES OF MIXED
VANADIUM CATALYSTS EZHKZI64ASA I
VANADIUM CATALYST FARB 62VC
THE PROCESS OF THE OXIDATION OF SULFUR-DIOXIDE WITH
VANADIUM CATALYSTS GEIREV56TPO
TEMPERATURE RELATION FOR THE RATE OF OXIDATION OF j
SULFUR-DIOXIDE ON VANADIUM CATALYSTS GEIBEV56TRF
EFFECT OF POTASSIUM-OXIDE ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE OXIDATION OF SULFUR-DIOXIDE AT LOW '
TEMPERATURES GFRBEV63EOP i
EFFECT OF SILICON-TETRAFLOURIDE ON A VANADIUM CATALYST
GERBEV63EOS
ALKALINE REGENERATION OF VANADIUM FROM SPENT CATALYST FROM
SULFURIC-ACID PRODUCTION GOLONA66ARO
THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH VANADIUM !
CATALYST HARAH 60TCO
VANADIUM COMPOUNDS AS CATALYSTS FOR THE OXIDATION OF
SULFUR-DIOXIDE HOLMHN30VCA
PHASE CONDITION OF ACTIVE COMPONENT IN VANADIUM CATALYSTS
OF SULFUR-DIOXIDE OXIDATION ILLAVV55PCO
KINETICS OF THE OXIDATION OF SULFUR-DIOXIDE WITH A POISONED
COMMERCIAL VANADIUM CATALYST I SHIT 65KOT
POISONING OF VANADIUM CATALYST IN A FLUIDIZED-BED WITH
ARSENIC-TRIOXIOE IVANPS62POV
VANADIUM CATALYSTS SUITABLE FOR USE IN OXIDATION OF
SULFUR-DIOXIDE JENKLE>5VCS
DATA FOR COMPUTATION OF VELOCITY CONSTANTS OF THE CATALYTIC
OXIDATION OF SULFUR-DIOXIDE ON VANADIUM CATALYSTS
JIRMP 5<*OEC
"4NAOIUM
PAGE 123
ELECTRON-MICROSCOPIC STUDY OF THE POROUS STRUCTURE OF A
VANADIUM CATALYST FOR SO? OXIDATION KARADB65EMS
THE OXIDATION OF GASES HIGH IN SULFUR-DIOXIDE AND OXYGEN IN
THE PRESENCE OF A VANADIUM CATALYST KIRRIP34TOO
EFFECT OF NUCLEAR RADIATION ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE REACTION OF SO? OXIDATION KOZAZ 66EON
VANADIUM CATALYTIC MASSES IN MANUFACTURE OF SULFURIC-ACI0
KRUME 41VCM
THE RATE OF OXIDATION OF S02 WITH INDUSTRIAL VANADIUM
CATALYST KUROH 5PTRO
ATTEMPTS TO INCREASE THE THERMAL RESISTANCE OF THE
INDUSTRIAL VANADIUM CATALYST IN THE REACTION OF OXIDATION
OF SO2 KUCZW S9ATI
ACTIVITY OF THERMALLY STABLE VANADIUM CATALYSTS FOR THE
OXIDATION OF SULFUR-DIOXIDE KUNITI63AOT
VANADIUM MODIFIED CRYSTALLINE ALUMINOSI LICATF.S AND THEIR
PROPERTIES LEVISA65VMC
OPTIMUM SHAPES AND SIZES OF FLEMFNTS OF A VANADIUM CATALYST
FOR THF. PRODUCTION OF CONTACT H2S04 MALKVI640SA
THE MECHANISM AND THE KINETICS OF SULFUR-DIOXIDE OXIDATION
ON CATALYSTS CONTAINING VANADIUM AND ALKALI OXIDES
MARSP fcBTMA
VANADIUM CATALYSTS FOR OXIDIZING SULFUR-DIOXIDE
META J7VCF
KINETICS OF SULFUR-DIOXIDE OXIDATION ON AN INDUSTRIAL
VANADIUM CATALYST MICHJ 67KOS
EFFECT OF WATER VAPOP AND IRON COMPOUNDS ON THE ACTIVITY
OF VANADIUM CATALYSTS IN A FLUIDIZED-RED MUKHIP63EOW
OXIDATION OF CONCENTRATED SULFUR-DIOXIDE IN A FLUIDIZED
LAYER OF WEAR RESISTANT VANADIUM CATALYST MUKHIP6.
POISONING OF VANADIUM CATALYSTS US?D IN THE OXIDATION OF
SULFUR-DIOXIDE IN A FI.UIDI ZEO-HE9 "IIJKHI PhSPOV
SOME RESULTS OF A STUDY QF ~ ~ '"
VANADIUM CATALYST
THE EFFECT OF THE CONCENTRATIONS CF IMPREGNATING SOLUTIONS
UPUN THE CHEMICAL COMPOSITION AND STRUCTURE OF A
MECHANICALLY STABLE VANADIU* CATALYST MiiKHiP65TEn
STRUCTURE OF WEAR RESISTANT VANADIUM CATALYSTS FOR
SULFUR-DIOXIDE OXIDATION IN A FLUIOIZED-BED
MIIKHI P67SWR
VANADIUM ON ALUMINA CATALYST FOR Fl UI DI ZED-BED OXIDATIONS
_NITT 65VOA
MUKHIP6500C
THE STRUCTURE OF A WEAK-RESISTANT
MUKHIP65RSS
VANADIUM CATALYSTS FOR THE PRODUCTION OF SULFUR I C-AC ID
OKAMT (-PVCF
THE MANUFACTURE OF SULFUR I C-AC ID BY MEANS OF VANADIUM
CATALYST ON AN IN TEP Me [) I &TF SCALE II. INCREASE OF THF
DRAFT RESISTANCE IN A SMALL CONVERTER OSAMG 34TMO
MANUFACTURE OF SULFtIK IC-AC ID BY VANADI U» CATALYST III
IMCREASF. OF THE DHAFT RESISTANCE IN THF LAHGF. CONVERTER
OSAMG 4T10S
THE IGNITION TEMPERA TlWES OF V4NAOIU" CATALYSTS
THE MECHANISM OF SULFUR-DIOXIDE OXIDATION IN THF I'PKSFNC.I- OF
VANADIUM CATALYSTS PPLYM
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10/27/6'J
VANADIUM
PAGE
THF OXIDATION OF GASES HIGH IN SULFUR-DIOXIDE AND OXYGEN IN
THE PRESENCE OF A VANADIUM CATALYST POSTVF34TOO
OPTIMUM DIMENSIONS FOR THE ELEMENTS OF A RING-SHAPED
VANADIUM CATALYST AND THE SEARCH FOR NEH GRAIN SHAPES
RITTLG6300F
VANADIUM CATALYSTS ON A BELAKS CARRIER FOR THE OXIDATION
OF SULFUR-DIOXIDE SALTVP63VCO
DATA CONCERNING THE BEHAVIOR OF THE VANADIUM CATALYSTS USED
IN ROMANIA SAMOI 6RDCT
RECOVERY OF VANADIUM FROM THE SPENT V-K SILICA GEL CATALYST
USED IN PHTHAL1C-ANHYDRIDE MANUFACTURING SHESAP65ROV
DETERIORATION IN SERVICE OF VANADIUM CATALYSTS USED FOR
.•OXIDATION OF- SULFUR-DIOXIDE SIROGO*8DIS
EFFECT OF CARRIERS ON THE ACTIVITIES AND PROPERTIES OF
VANADIUM CATALYSTS FOR THE OXIDATION OF -SULFUR-TRIOXIDE
SOLOBI64EOC
THE INFLUENCE OF THE CARRIER ON THE ACTIVITY OF THE VANADIUM
CATALYSTS FOR THE OXIDATION OF SULFUROUS-ANHYDRIDE
SOLOBI64T|n
VANADIUM CATALYST USED IN THE OXIDATION OF S02 EFFECT OF
MECHANICAL TREATMENT OF CARRIER ON THE ACTIVITY OF CONTACT
OXIDATION OF SULFUR-DIOXIDE IN A FLUIDIZED BED
OP
CATALYST
TIMUM SHAPE
SZC1LP 55005
A VANADIUM CATALYST
EFFECT OF VANADIUM PEN.TOXIOE ON GAS-PHAS
CARBON-MONOXIDE SULFUR-DIOXIDE OXYGEN
EFFECT OF PARTICLE
ACTIVITY IN
AND GRAIN SIZE FOR _
TEREOF630SA
COMBUSTION 1 THE
YSTEM
TIPPCF64EOV
A VANADIUM CATALYST ON ITS
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THE~FLlllDIZED-BEbi OXIDATION "OF "
VANADIUM-BAR IU««
VANADIUM-BASE
VANADIUM-GXIOE
SWINA 66VCU
WITH VANADIUM
OXIDATION OF SULFUR-DIOXIDE ON FLUIDIZED VANADIUM CATALYS
VARLML5400S
NEW VANADIUM CATALYST VFB 65NVC
VANADIUM CATALYSTS ON SILICA VEB A5VCO
THERMOGRAPHIC DETERMINATION OF THE IGNITION TEMPERATURE FOR
VANADIUM CATALYSTS VISHIV61TDO
RECOVERY OF VANADIUM FROM PETROLEUM WHICH 67ROV
KINETIC STUDIES OF THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYSTS PROMOTED BY ALKALI METAL SALTS
ZAKHMS5SKSO
ACTION OF HYDROGEN-FLOUR IDE ON THE VANADIUM-BARIUM CONTACT
MASS FOR THE OXIDATION OF SO? ADADIEITAPH
PREPARATION OF VANADIUM-RASE CATALYSTS FOR THE SULFURIC-ACID
INDUSTRY OIACV 55POV
OXIDATION CARRIED OUT RY MEANS OF VANAOIUM-OXIDE CATALYSTS
MARSP
THERNOGRAPHIC STUDY OF THE CATALYTIC OXIDATION OF
SULFUR-DIOXIDE ON VANAD|UM-OXIOf SATAV
10/27/ft<3
VANADIUM-OXIDE
PAGE 125
CATALYTIC PROPERTY OF VANADIUM-OXIDE IN THE REDUCTION OF
VANAO.UM-PENTOXIDE
VANAD,UM-OX,OEVICSCATV!tYiTP°
VOLFVY65SCV.
SULFUR-OX I OF
EFFECT OF THE ALKALI
VANADIUM-PENTOXIDE
SULFUR-OXIDE
SEMICONDUCTING PROPERTIES OF VANADIUM-PENTOXIDE AND THE
CATALYTIC OXIDATION OF SULFUR-DIOXIDE BUTLJD60SPO
A NEW MECHANISM FOR THE ACTION OF THE VANAOI UM-PENTOXIDE
SILICA-ALKALI PYROSULFATE CATALYST FOR THE OXIDATION
OF SULFUR-DIOXIDE FRAZJH40ANM
REACTION RATES OF CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH
VANADIUM-PENTOXIDE CATALYSTS HARAH 59RRO
THE INFLUENCE OF SHALL QUANTITIES OF ADDED PLATINUM ON THE
CATALYTIC ACTIVITY OF VANAOI UM-PENTOXIOE REGARDING THE
OXIDATION OF HYDROGEN ILCHNI67TIO
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVITY OF
VANAOIUM-PENTOXIOE IN THE CATALYTIC OXIDATION OF
-------- ------ JIRUP 63EOT
METAL SULFATES ON THE ACTIVITY OF
IN THE CATALYTIC OXIDATION OF
____ ... ______ JIRUP 63VPC
THE. INFLUENCE OF CARRIERS ON THE CATALYTIC PROPERTIES OF
VANADIUM-PENTOXIDE KARMM034TIO
ISQTOPF EXCHANGE FOR THE OXYGEN OF VANADIUM-PENTOXIDE WITH
SULFUR -01 OX IDE AND TRIOXIDE KASALA6MEF
THE INFLUENCE OF CARRIERS ON THE CATALYTIC PROPERTIES OF
VANAOIUM-PENTOXIOE KHAROH3*TIO
CATALYTIC ACTIVITY OF VANADIUM-PENTOXIDE CATALYST ON
KUBOT 54CAO
THE ROLE OF THE OXYGEN OF VANADI UM-PENTOXIOE CATALYSTS IN
THE CATALYSIS OF OXIDATION ROITVA5BTRO
KINETICS OF SULFUR-DIOXIDE OXIDATION ON VANADI UM-PENTOXIOE
STADVP64KOS
EFFECT OF GAS ENVIRONMENT ON CERTAIN SEMICONDUCTOR
PROPERTIES OF VANADIUM-PENTOXIDE SURNLN&SEGE
ACTIVITY OF PURE VANADIUM-PENTOXIDE IN CONTACT OXIDATION OF
S02 WEYCS 6SAOP
VANADIUM-SILICATES
COMPOSITION OF VANADIUM-SILICATES AS INVESTIGATED BY
ELECTRON-PARAMAGNETIC-RESONANCE HOREGK66COV
VANADIUM-SULFUR 1C- AC ID
THE HEATING-UP TEMPERATURE OF VANAOI UM-SULFURI C-ACI 0
CATALYST BORFGK49THU
VANADVL-SULFATE
THE ROLE OF VANADYL-SULFATE IN THE PROCESS OF CATALYTIC
OXIDATION OF SULFUR-DIOXIDE WEVCS 55TRO
VAPOR
INVESTIGATION OF THE MECHANISM OF OXIDATION HVOROGENATION
AND ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS
OXIDATION OF SULFUR DIOXIDE ON
IN THE PRESENCE OF WATER VAPOR
EFFECT OF WATER VAPOR AND IRON COMPOUNDS ON THE ACTIVITY
OF VANADIUM CATALYSTS IN A FLUIOIZED-RFO MUKHI P63FOW
ACTIVATED CARBON AT 20-DEG
OAVTOKMIMn
159
160
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1C/27/69
VAPOR
VAPOR-PHASE
VAPORS
VELOCITY
VENTURI
VIBRATION
VISCOSITY
V205
RADG 64AFV
METT 6ACVG
ROTGH 26GOV
PAGE 126
REDUCING DISCHARGE INTO THE ATMOSPHERE OF SULFUR IC-ACID HIST
MINIMIZING SULFURIC-ACID VAPOR DISCHARGE INTO THE
ATMOSPHERE ZILRDE68RDI
APPARATUS FOR VAPOR-PHASE CATALYTIC REACTIONS
CATALYTIC VAPOR-PHASE GAS CLEANING
GAS OR VAPOR-PHASE CATALYTIC PROCESSES
EQUILIBRIUM PRESSURE OF SULFUR-TRIOXIDE VAPORS OVER OLEUM
AKSEYV64EPS
EFFECT OF WATER VAPORS ON THE REACTION OF SODA WITH
SULFUR-DIOXIDE AT TEMPERATURES ABOVE 100-DEGREES
Cpr
DETERMINATION OF TRACES AND THE MICROANALYSIS OF GASES
AND VAPORS HARM 66DTH
PROCEDURES AND INSTALL*TIONS FOR NEUTRAL/ZING TOXIC VAPORS
AND WASTE GASES REUBF 67OIN
CHROMIUM-VANADIUM CATALYST WITH A HIGH VELOCITY CONSTANT
4DAOIE3TCVC
EFFECT OF A POROUS SILICA-GEL CATALYST CARRIER ON THE
~ ~;ITY OF OXIDATION " "'" "
VELOCI
OF OXIDATION OF SULFUR-DIOXIDE GAS
CHUFGI34EOA
THE VELOCITY OF ACID FORMATION IN THE PRESENCE OF SALTS. IN
NITROSE
GLAOVI63TVO
AND WATER SOLUTIONS OF SURFACE ACTIVE AGENTS
DATA FOR COMPUTATION OF VELOCITY CONSTANTS OF THE CATALYTIC
OXIDATION OF SULFUR-DIOXIDE ON VANADIUM CATALYSTS
JIRUP 59DEC
ON THE ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE
SOLUTION IN A VENTURI ABSORBER ELEND 66ASO
HYDRODYNAMICS AND MASS TRANSFER IN A NOZZLELESS VENTURI
ABSORBER. ABSORPTION OF SULFUR-DIOXIDE INTO WATER
RFACE ACTIVE AGENTS
ELEND 66HMT
GAS ABSORPTION BY MULTISTAGE VENTURI SCRUBBERS
VOLGBP64GSM
ABSORPTION OF SULFUR-DIOXIDE BY AMMONIUM-SULFITE-BISULFITE
SOLUTIONS IN A SPRAY TYPE VENTURI SCRUBBER VOLGBP6&ASD
ACCELERATIONS OF CHEMICAL REACTIONS BY VIBRATION
STELP053AOC
VISCOSITY AND INTERMOLECULAR POTENTIALS OF HVDROGEN-SULFIDE
SULFUR-DIOXIDE AND AMMONIA DAL AK&7VIP
DEPENDENCE OF THE CATALYTIC ACTIVITY OF THE
V205 ON ITS MODE OF COMBINATION WITH SILICA
ADADIF24DOT
INFLUENCE OF ALKALI SULFATFD ON THE ACTIVITY OF
V205 IN THF CATALYTIC OXIDATION OF SULFUR-DIOXIDE
JIRUP 6"IOA
1C!
10/27/69
V205
WEAR-RESISTANT
WORK-FUNCTION
X-RAY
YIELD
ZEOLITES
ZINC
ZIRCUNIUH
PAGE 127
EFFECT OF ALKALI METAL Sill FATES ON THF ACTIVITY OF
V205 FOR THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
JIRUP 61EAM
SOME RESULTS OF A STUDY OF THE STRUCTURE OF A WEAR-RESISTANT
VANADIUM CATALYST MUKHI P65RSS
CHANGES IN THE I
ELECTRON UPON
CONDUCTIVITY AND WORK-FUNCTION OF
ABSORPTION OF 0 AND SO2 AND V20S
SPECTROGRAPHIC AND X-RAY DIFFRACTION STUDY OF
CATALYST FOR SULFURIC-ACID MANUFACTURE
EFFECTS OF X-RAY IRRADIATION ON THE OXIDATION
SULFUR-DIOXIDE BY VANADIA-TITANIA CATALYSTS
THE
LAYERS
SURNLN65CIT
IRON-OXIDE
K07HNV66PAX
OF
EFFECT OF IONIZING RADIATIONS ON THE SULFUR-OIOXIO£-OXYGEN°X
SYSTEM I I THE OXIOATION OF SULFUROUS-ACI 0
BY ACTION OF X-RAY RADIATION
OF
TO
SULFURIC-ACID
SCHRR 64EO!
INCREASE OF THF YIELD OF S03 IN THF CATALYTIC OXIDATION OF
THE LAW OF MASS-ACTION AS THE BASIS FOR CALCUL AT I N^THF^BF ST
YIELD FROM TECHNICAL AND ECONOMIC STANDPOINTS
SAVEW 52TLO
SYNTHETIC ZEOLITES OFFFR UNIQUE PROPERTIES AS CATALYST
SUPPORTS STORDH64SZO
ZINC RECOVERY AT CANADIAN
VALLEYFIELD PLANT
ELECTROLYTIC ZINC'S NEW
JF.PHAC66ZRC
ACTION OF SULFUR-DIOXIDE ON TITANIUM ZIRCONIUM HAFNIUM
VANADIUM NIOBIUM AND TANTALUM DAVIL 62ASD
1G2
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RECOVERY OF VANADIUM FROM THE CATALYST USED IN THE CONT
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"AGE
10/27/69
pace
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ALCAG 6*ci?T ALMASSEY G /AOOR G
" " COMPLETION OF rut nxrOATION OF S02 CATALYST FU°NACE OF A NEW
TYPE IN A H2S04 PLANT
"AGY. KEM. LAPJA 131 1 0 ) , '.73-80 1 1 963 ) CA-6S-10252 D
AMARAP65RPP AM ARYAN AP 8A7. 1 LF VSK I I VM nROZOOVSKII EF
RECOVERY OF PRECIOUS METAL PLATINUM FPHM ALUMINOUS
CATALYSTS AND WASTES
U.S.S.R. 171,116 (CL. C 228), MAY 1 1 , 1965, APPL. APRI L 17,196*
CA-63-(P)-12729 0
AMARAP66RQP AMARYAN AP 8A7. ILFVSKII VM OROZDOVSKIl EE
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U.S.S.R. 190,874 (CL C 018) JAN. 14, 1967.APPL.OCT.3P ,1965
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STABILITY IN DISTRIBUTED PARAMETER SYSTEMS
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PREPARATION OF OLEUM
U.S.S.R.186,«02 (CL. C OIBI,OCT.3,1966.APPL.NOV.19,1963
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EQUILIBRIUM POSITION AND KINETICS OF OXIDATION OF
ANORL 62AOT
ANOK 65CFF
ANON 66NPP
APAKIA65IOC
SULFUR-DIOXIDE AND SYNTHESIS OF AMMONIA
GENIE CHIM. 85,103(1961) CA-55-21499 H
ANDRUSSOV L
ASPECTS OF THE-KINETICS OF FAST CATALYTIC REACTIONS
OECHMA MONOGRAPH 42,NO.661-76,87-96(1962) CA-59-66 F
ANOKHIN
CALCULATIONS FOR FLUIDIZED BED CATALYTIC EQUIPMENT
I1ZV..yYSSHIKH.yCHEBN._ZAyEDENII,KHIH I KHIM "
CA-64-12210 F
876-8(1965) RUSS
ANON
NEW PILOT PLANTS TACKLE S02 POLLUTION
CHEM.ENG. NEWS 44(271,36-811966)ENG CA-65-R-7887 F
APAKHOV IA PARYLIS EY KLYUKINA EP
KALYZINA VS POSTNIKOVA AV
IMPROVED QUALITY OF CONTACT OF SULFURIC-ACID
KHIM. PROM. 41110),745-611965IRUSS CA-64-30920
TECHNOL.8I5)
APAKIA66PFS APAKHOV IA
U.S.S.R. 182.699 (CL
CA-66-1PI-20640 Z
BULYCHEVA LI FEDIN VN
~"OM OF SULFURIC-ACID FOG IN
-ACID MANUFACTURE
C OIB),JUNE 9,1966,APPL. JUNF 20,1964
PREVENTING THE FORMATION OF SULFURIC-ACID FOG IN THE CONTACT
PROCESS FOR SULFURIC-ACID MANUFACTURE
ARAIK 67APC
ARGOWB53AOS ARGO MB
ASENJ 67SCC
ARAI K
AIR POLLUTION CONTROL
NENRYO KYOKAISHI 46(48
IN PETROLEUM REFINERIES
51,669-79(19671 JAPAN CA-67-8117O
SMITH JM
ACTIVITY OF SOLID CATALYSTS
IND.ENG.CHEM. 45.298-302(19531 CA-47-418P E
AS ENS J MOLINA J
STRUCTURAL CHARACTERIZATION OF CATALYSTS
OF MERCURY
AFINIDAD 24(250).274-5(1967ISPAN
PORROSIMMETRY
ASENJ 67SCP ASENS J
_ MOLINA J
STRUCTURAL CHARACTERIZATION OF CATALYSTS
OF DATA ON GAS ABSORPTION
AFINIDAD 24(250, 267-73< 19671SPAN.
INTERPRETATION
DIFFUSION TUBES
Z.ELEKTROCHEM.57,93«-'i3l
CA-48-5626 I
ASPEK 64NDI ASPERGER K
NEW DEVELOPMENTS IN THE TECHNOLOGY C1F SULFUR IC-AC 10
CHEM, TECH.(BELIN) 1 61 6) , 346-531 1964) CA-61-10343 C
ASPEK 64ND1 PRODUCTION
AXtLKO66ASD AXELSSON KO
ABSORPTION OF SULFUR-DIOXIDE AND SEPARATION OF ASHES FROM
COMBUSTION GASES OBTAINED BY COMBUSTION OF MAGNESIUM WASTE
LYE
U.S. 3,261,662 (CL. 23-48), JULY 19, 1966, APPL. MAY 3, 1963
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AXELK066ASO
AZOUA 64PSP
BACHG 34COO
RADG 64AFV
CA-65-P-H829 C
AZOULAY A SOLINHAC J
PURIFICATION OF SULFIJROUS RESIDUAL GASES BY ALUMINA BED
GAS(ROME) 14C 11I.351-8I1964MTAL CA-64-4645E
BACHALARt
CATALYTIC
INDUSTRIE
OXIDATION OF SULFUR-DIOXIDE
CHIMIOUE 22.408-171 19351 CA-29-6370-4
CATAL¥TIC REftCT10NS
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HADISCHE ANILIN-6 SODA-FABRIK A.-G.
VANADIUM CATALYST FOR OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIOE
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.27,I 964,APPL.AUG.16,1962
OXIDATION OF REDUCED CATALYSTS
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CA-6l-(P)-126B7 C
BAERE 26CSD
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RAERWALD E GOLDNANN H
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GER. 539,571,FEB. 11.1928 CA-26-(PI-2285-6
BAKER C CO. INC
BRIT.V594,461,NOV.12;1947~CA-42-«Pl-241C-H
GAS-THERMAL-CONDUCTIVITY STUDIES AT TEMPERATURE RESULTS
PHYS? FLUIDS 7(91,1400-2(196*1 CA-61-12668 A
EXPERIMENTAL REACTORS FOR CONTACT CATALYSIS
MAGYAR KEM. LAPJA. 2012),57-6511965)HUNG. CA-65-76 G
DEVELOPMENT OF CONTACT CATALYTIC REACTORS
MftGY.KEM.LAPJA.22«7|.366-70(1967IHUNG. CA-67-83266Y
NEW*DATAAON THE HULTIPLET THFOPY OF CATALYSIS
CATALYSIS CHEM.KINET. 1964, 33-5(?(ENGIC A-66-5921 3 N
BALAAA67AAE BALADIN AA SdTSYN VI BARSQVA LI
AGRONOMOV AE DOBR1SF.L • SKA YA NP
ADSORPTION AND ENERGETIC PROPERTIES OF METALLIC CATALYSTS
ZH.FIZ.KHIM.4l( 101,2623-811967IRUSS CA-68-33604 G
BALAAA67AEP BALANDIA AA SPfTSYN VI BARSQVA LI
AGRONOMOV AE DOHROSEL•SKAYA NP
ABSORPTION AND ENERGETIC PROPERTIES OF METALLIC CATALYSTS
SPECIFIC SURFACES OF CATALYSTS
ZH. FIZ. KHIH. 41(101. 2623-811967IRUSS CA-68-33604 G
BALOJ 66CR
SDLDAN J
SYPTAK K
BALOS J
FORMANEK I
CATALYTIC REACTOR
CZECH. 120,720 1C.9 B 01J,.NOV.15,1966.APPL.MAY 26.1965
CA-68-( PI-23031 D
BARNHE&6MRK BARNER HE PIGFORD RL SCHREINER WC
A MODIFIED REDLICH-KWONG EQUATION OF STATE
AK. PETROL. INST. PREPRINT NO.3811966)ENG CA-65-14449 H
BARNS TONE LA
THFEL5Igf?ES-SBtSDRi2^ggL °F ^ f"°THER"" REACTION IN A
^lERTjT?oSFAB5iR&r26?l?R3?8C3V!9g5?I5GN8A-6l:,!7g2g'277PP
BAROT 52RKI BARON T
BARTJ 64VC
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MANNING HR
JOHNSTONE HF
REACTION KINETICS IN A TUBULAR REACTOR
CHEM.ENG.PROGRESS 4B, 12*- 32U952 ) CA-46-3B41-G
BARTOS J
VANADIUM CATALYSTS
CZECH,HI, 1321 CL. B 01I.C C1B),JUNE 15.1964 CA-62-1 P)-2529 H
RARU VG VOL'KENSHTEIN FF
POSSIBLE MECHANISM OF THE EFFECT OF RADIOACTIVE ADDITIONS
'"10 AN" CHEHISORPTIVE "OPERTIES OF
Z.PHYS IK. CHEN. (LEIPZIG) 228(3/4), 193-205119651 GER.
BASOVA66IER RASOV VA MARKHFVKA VI MFL IK-AKHNAZAROV TK
INDySTRlALTEFFECTIVENESS OF REACTORS WITH FLUIOI ZED-BEOS OF
KH1M.PROM. 421 6), 439-431 1966IRUSS CA-65-1651B H
BASSL°17PAA
BAUHM 66RER
BASSFT_LP
SWISS 74,444 JULY "1671917
PROCESS AND APPARATUS FOR OXIDIZING SULFUR-DIOXIDE
n, t r r -m , * * * ...... . , ...... — 1?— (PI— B3 — Q
BAIIMANN M
"UPES.Z
POHL J
RUZICKA R
BlIRANEK F
ZIVOTSKY K
SFFCIK M
JAVUREK V BUR.
REACTOR FOR EXOTHERMIC REACTIONS AT ELEVATED TEMPERATURE AND
PRESSURE
CZECH.121, I82ICL B OIJ I .DEC . 1 5, 1966 . APPL90CT.3 ,1 962
CA-68-CP 1-23030 C
:.C9
.'.70
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PAGE
BAURK 44TNO BAUR E
THE NATURE OF BAUR•S KINETICS
VIERTELJAHRSSCHR. NATURFORSCH. GES. ZURICH 89. BEIHFFT MO. 1
51 PPU944) CA-40-4940-2
BAYEJ 35COE BAYER J HENECKY K
CARRYING OUT EXOTHERMIC CATALYTIC GAS REACTIONS SUCH AS
OXIDATION OF SULFUR-DIOXIDE
US. 2.029,60* FEB.4 CA-30-(P)-1616-8
3ELDDH65SSC BFLOEN OH
STORING AND STRIPPING CATALYST IN A FLUIOIZFD SYSTEM
U.S. 3,208,831 ICL. 23-288 I,SEPT.28,1965.APPL.JULY 31.1961
CA-63-1 PI-17206 C
BELEIM61CBO BELEN'KAYA IM
CATALYSTS BASED ON ION-EXCHANGERS
1SSLEO. V OBLASTI PROM. PRIMENEN. SORBENTOV.AKAO.NAUK SSSR
OTO. KHIM.NAUK 1961 2GR-71 CA-56-14972 F
BELLTN55TKO SELL TN ROBINSON PL TRENHITH AB
THE KINETICS OF THE OXIDATION OF SULFUR-DIOXIDE BY
NITROUS-OXIDE
J.CHE1. SOC. 1955.1440-4 CA-49-12092 D
BHRTRJ6"5NMR BERTOLACINI RJ
NOBLE METAL RECOVERY PROCESS
US. 3,169,056 (CL.75-83),FEB. 9,1965,APPL.MAR.18.
CA-62-IPI-10272 C
3ESKVS63DOC HESKOV VS BU7.HOAN YM SLIN'KO MG
DESIGN OF CONTACT PROCESS EQUIPMENT WITH AN AOIABATIC
CATALYST LAYER FOP. THE OXIDATION OF SULFUR-DIOXIDE DESIGN
OF EQUIPMENT WITH THE INTRODUCTION OF COLO REACTION
MIXTURES AND WITH INTERMEDIATE HEAT EXCHANGERS •
KHIM.PROM. 1963(101.721-4 CA-60-B913H
SLIN'KO MG
BESKVS64DOT BESKOV VS LIBERZON LM SL. _ _
DETERMINATION OF THF STATIC CHARACTERISTICS OF A CONTACT
REACTOR FOR THE OXIDATION OF SULFUR-DIOXIDE WITH THE AIM
OF OPTIMIZING THE PROCESS
KHIM.PROM. 1964(9)678-80 CA-61-15686A
SLIN'KO MG
BOBYLEVA IM
BENNRL63TRC BENNETT RL
KEILHOLTZ
THERMAL RADIATION AND CHEMICAL STABILITY OF SULFUR-DIOXIDE
U.S. AT.ENERGY COMM.ORNL-TM-747(1963) CA-61-9167 H
BESKVS650OC BESKOV VS . ... ._
DESIGNING OF CONTACT APPARATUS FOR THE OXIDATION OF
DIOXIDE
MODELIR. I OPTIMIZ. KATALITICH. PROTSESSOV,SB 1965,74-87
RUSS CA-65-14882 F
BETTJ 60ASD gETTELHEM Jp ^ RjRKL {-EC EK RN ^ ^^ ^^ ^^ JETS
CHEM. PRUMYSL 10661,281-4(1960) CA-61-10338H
BERAL 67ACB BERAMEK L
NOMALI-Z _
COURSE OF
ANOMALIES CAUSED BY THE SLOW ADSORPTION OF
:_,RSE OF CERTAIN TYPES OF CONSEC "
HETEROGENEOUS CATALYTIC REACTIONS
.._ . _. A REACTANT ON THE
OF CONSECUTIVE AND BRANCHED
BFTTJ 65MCS BETTELHEIM J
KLIMECEK R
FRANTISAK F
DERKA J
32(2) ,484-5041 1967IENG
COLLECTION CZECH. CHEM. COMMUN.
CA-66-59250 X
BERAV 57TMO SULFUR-DIOXIDE
KHIM.PROM. 1957,42-3 CA-51-11021 A
BERAY 57TUO BFRANEK Y KLUMPAR I
THE USE OF FLUIDIZED CATALYST FOR THE OXIDATION OF
BERG 63DFG BERGWESKSVERBANO
OESULF'JRIZING FINE GASES
NETH. »P»L. 6,409,706 (CL. B DID) ,FEB. 24, 1965.GFR. APPL.
AUG.23, 1963 CA-M-P-1637 A
BERG 67SSO BERGWERKSVERBAND
SEPARATION OF SULFUR-DIOXIDE FROM WASTE GASES
BRIT. 1.090.306 (CL.C 0 IB(NOV.8.1967 GER.APPL SEPT 16,1965
CA-68-(P)-42930 N
BERGP 57PCO BERGAN P
PROBLEMS OF CORROSIONS AND DEPOSITS ON THE FLUE-GAS SIOE
OF HEATING SYSTEMS
TFK UKEBLAD 104 B1-7UQ57) CHEM.ZENTR. 1 29,256 (1 9S8 >
CA-53-19814 B
MANUFACTURING CONCENTRATED SULFUR-DIOXIDE FRO" INDUSTRIAL
WASTE GASES BY THE AMMONIUM CYCLIC METHOD
CZECH.114,564 (CL. C ."MBI.MAY 15,1965 APPL. SEPT.4,1962
CA-64-15440A
RRUNIM LW
MURPHY EM
BIEND 58SDC BIENSTOCK n
BFNSON HE
SULFUR-niOXIDE ITS CHEMISTRY AND REMOVAL FROM INDUSTRIAL
WASTE GASES
US.BUR.MINES,INFORM.CIRC.NO. 7R36 1958-CA-52-176?
BIEND 60BSI BIENSTOCK II FIELD JH
BENCH-SCALE INVESTIGATIONS ON REMOVING SIILFUR-01CX IDF-
J. AIR POLLUTION CONTROL ASSOCN 10-121-5(1960) CA-54-135"9F
BIEND 64RSD OIFNSTOCK 0 FIELC
REMOVAL OF SULFUR-OIOXIDt
U.S. 3.15.1,923 (CL. 23-2),SEPT. 29,1964, APPL. JAN 18.1962
CA-61-(PI-16694E
I ELD JH
XIDE FROM GASES
FIELD JH
KATELL S
HI TNI 65F.IIP HIENSTtKK D
PLANTS KD
EVALUATION OF DRY PROCPSSFS FOR HF MOVING SO2 FROM POWFR
PLANT FLUE RASES
J. AIR POLLUTION CONTROL 1 51 10 I . 459-64 (1 965) ENf, CA-64-1873 C
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11
(>7PDP HIENSTnCK n FIELD JH 1YFRS JG
"•POCF.SS DEVELOPMENT IN REMOVING SULFUR-DIOXIDE FROM HOT
FLUE GASES PILOT PLANT STUDY OF THE ALKALIZED
ALUMINA SYSTEM FOP SULFUR-DIOXIDE REMOVAL
U.S. BUR. MINES, REP. INVEST. NO. 7021 (1967)ENG.
CA-67-H010B G
BILLBH66CSD BILLINGE BH
THE CHEMISORPTION OF SULFUR-DIOXIDE ON CARBONS
CGNF. INO. GRAPHITE.PAPERS,2ND,LONDON 1965.398-40*
PURL 1466 (ENG) CA-66-B8903 T
BILLJ 67PHD BILLY J
POROUS-BED DIFFUSION USING THE FREQUENCY RESPONSE METHOD
COMMIS ENERG.AT.IFR.IRAPP.CEA-R 3370,15(1967)FR.
BISCKB65EFF HISCHOFF KR
EFFECTIVENESS FACTORS FOR GENERAL REACTION RATE FOPMS
A.I.CH.E.J. 11121,351-5( 1965IENG CA-63-1492 B
HISKE 67RFT B1SKIIPSKI E STASZKO M
REACTOR FOR THE OXIDATION OF AMMONIA
SZPARAGO J
POL.53,366 ICi; c'"6lb) ~ JUNE*' 10. 1967,APPL. APRI L 2,1965
CA-6B-IP)-41456 A
BLASH 66ASO BLASINSKI H IGNACZAK M
ABSORPTION OF SULFUR-DIOXIDE BY SODIUM-CARBONATE AQUEOUS
SOLUTION FROM A GAS MIXTURE
POLITECH., LODZ, POLAND. PRZEMYSL CHEM. 45(7), 374-8(1966)
POLAND CA-65-14876 A
BLICT 610SD RLICKLE T JONGE J • FERENCZY I
OXIDIZING SULFUR-DIOXIDE BY USING FLUIDIZED IRONIIII) OXIDE
VESZPREMI VEGYIP.EGYET. KOZLEMEN. 5, 109-2P>( I 961) CA-57-4090 F
BLIZG 65AIf BLIZNOKOV G
ASPECTS IN THE INVESTIGATION OF ADSORPTION AND CATALYTIC
PROCESSES
CHIM. CRONIKA(GREECE I 30171,112-1911965)ENG CA-63-14097 A
BLOCJ 56SOM BLOCK J
SELECTION UF MATERIAL FOR CONTACT CATALYSTS BEHAVIOR AND
PROPERTIES OF SEMICONDUCTING CATALYSTS
WERKSTOFFE U. KORROSION 7,127-37(19561 CA-50-17255 G
BLUMH 66DOP
BLUHE H
KLOTZSCHE H
WEIDENBACH G
SZKIBIK C
STRICH ER
PFEIFFER F
BECKER K
DAMAGING OF PT CATALYSTS IN INDUSTRIAL USE
CHFM.TECH.(BERLIN) 1819),449-54(1966IGEP.CA-65-19347 D
1G ZHIVAIKIN LY YUROVSKAYA NA
1
IV
BLYAIG66AST BLYAKER
AVD6EVA ..
ABSORPTION OF SULFUR-TRIOX IDF IN A FI1AM TYPE APPARATUS
HAVING AN INTERNAL ML1* HEAT TRANSFER DEVICE
KHIM.PROM. 421 3), 17R-BII I966)RUSS
ROGDGA58TMO BOGDANOVSKI I GA SHIGIN AI
THE MECHANISM OF THE ELECTROLYTIC OXIDATION OF
SULFUR-DIOXIDE
ZHUR.FIZ.KHIM. 32, 418-21 195HO CA-52-14388!
BOGOML46IAH BOGOYAVLENSKAYA ML KOVAL'SKII AA
INITIATING A HOMOGENEOUS REACTION IN A GAS BY SOLID CATALYST
J.PHYS.CHEM.(U.S.S.R.I 20.1325-311 1946) CA-41-2972
BONDGC65SPM BOND GC SERCDMBE EJ
SUPPORTED PLATINUM METAL CATALYSTS THEIR SELECTION AND
METHODS OF USE IN INDUSTRIAL PROCESSES
PLATINUM METALS REV. 9(3i.74-9(i965)ENG CA-63-10739 o
BOREGK33TKO BORESKOV GK PLIGUNOV VP
THE KINETICS OF THE CONTACT OXIDATION OF SULFUR-DIOXIDE
J.APPL. CHEM. (USSR) 6,785-96(1933) CA-28-4181
BOPEGK35VCF BORESKOV
VANADIUM
KOV Gl
IUM C
•yj *
TRANS.V. _..
159-66(1935)
ATALYZERS FOR SULFURIC-ACID PRODUCTION
THEORE1
ENDELEFL CONOR.
-- -A-29-6371-9
EORET.APPLIED CHEM. 1932 2.PT. 1
BOREGK37TOC BORESKOV GK SOKOLOVA Tl
THE OPTIMUM CONCENTRATION OF SULFUR-DIOXIDE IN CONTACT
SULFURIC-ACID PRODUCTION
J.CHEM.IND.(U.S.S.R) 14,1241-50(1937) CA-3Z-1963-3
BOREGK40MOO BORESKC1V GK PL IGUNOV VP
MECHANISM OF OXIDATION OF SULFUR-DIOXIDE IN THE PRESENCE
OF ACTIVATED VANADIUM CATALYSTS INFLUENCE OF AN
ADMIXTURE OF SALTS OF ALKALI ELEMENTS AND AMORPHOUS
J.APPL.CHlMIUSSR) 13,653-61(1940) CA-35-3396-7
BOREGK40MOT BORESKOV GK
PLIGUNOV VP
MECHANISM OF THE OXIDATION OF SULFUR-DIOXIDE IN THE PRESENCE
OF ACTIVATED VANADIUM CATALYSTS STABILITY OF VANADIUM
COMPOUNDS UNDER THE CONDITION OF SULFURIC-ACID CATALYSIS
J.APPL.CHEM(USSR 113,329-35(1940) CA-34-8185
BOREGK44KOC BORESKOV GK SOKOLOVA T!
KINETICS OF CONTACT OXIDATION OF SULFUR-DIOXIDE IN THE
PRESENCE OF FERRIC-OXIDE
J.PHYS.CHEM (U.S.S.R.>18,87-101<1944) CA-40-52ll-9
BOREGK45KOT BORESKOV GK
KINETICS OF THE CONTACT SYNTHESIS OF SULFURIC-AC ID
J.PHYS.CHEM.(U.S.S.R.)19,535-50(19451 CA-40-2943-8
ROPEGK45RBR BORESKOV GK
RELATION BETWEEN REACTION ORDER AND ENERGY OF ACTIVATION
OF DIRECT AND INVERSE REACTIONS
J.PHYS. CHEM.(U.S.S.R.I 19,92-5(1945) CA-39-3719-2
773
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13
BORET.K47STP BORESKOV GK RITTFR LG SERERRENNIKOVA MT
SULFUR-TRtnXIDE PRODUCTION WITH OXYGEN BY THE CONTACT METHOD
KHIM.PROM.1947,ND.1,8-12 CA-50-16C54 D
BOREGK49THU BORESKOV GK RITTFR LG VOLKOVA El
THE HEATING-UP TEMPERATURE OF VANAOIIJM-SULFURI C-AC ID
CATALYST
ZHUR.PRIKLAD.KHIM (J.APPL.CHEH)22,750-6011949) CA-43-8251-G
BOREGK52KOR BORESKOV GK SLIN'KO MG
KINETICS OF REVERSIBLE CATALYTIC REACTIONS IN THC INTERNAL-
DIFFUSION RANGE
ZHUR.FIZ.KHIM.26,235-B(1952) CA-47-4714-1
VOLKOVA F.I
SULFUR-TRIOXIOE BY METALS AND
BOREGK53COS BGRESKHV GK • SLIN'KO MG
CATALYSIS OF SULFUR-DIOXIDE TO .. _.
PLATINUM-GOLD ALLOYS
OCKAOY.AKAD.NAUK S.S.S.R 92,109-10(1953) CA-50-3863 A
BOREGK53COT BORESKOV GK SLIN'KO MG VOLKOVA El
CATALYSIS OF THE CONVERSION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE BY MFTALS AND PLATINUM GOLD ALLOYS
DOKLADY AKAD. NAUK SSSR. 92, 1T9-101 1953 ) CA-50-386? A
BOREGK56MQA 8CRESKOV GK
MECHANISM OF ACTION OF SOLID CATALYSTS
GETERfiGENNYI KATALIZ V KHIM V KHIM. PRPM. SBORNIK 1955,5-28
RFFERAT ZHUR.KHIM.1956.ARSTR.NO.32013 CA-52-179?21
BOREGK6000C BCRESKOV GK SLIN'KO MG
OPTIMIZATION OF CATALYTIC PROCESSES IN INDUSTRIAL REACTORS
KHIM.PROM.I960,NO.3.193-201 CA-54-734H2 E
HOPFGKfr4SBS BORESKHV GK
SCIENTIFIC BASES FOR SELECTING AND PREPARING CATALYSTS
NAUCHN. OSNOVY.POOBORA I PRQIZV. KATALIZATOROV,AKAD.NAUK
SSSP,STBIRSK. OTO. 1964,7-20IRUSS) CA-63-4985H
BOREGKfr4SPO BCRFSKOV GK
Sr*E PRDRLEMS OF CATALYST SELECTION
CATALYSIS CHEM. KINET.1964,59-74(CNGI CA-66-59214 P
ROREGKt4TS3 BOPESKOV GK
ThEQPETICAL SELECTION PREPARATION AND USE OF INDUSTRIAL
CATALYSTS
PRC1C. INTERN.CONGR. f.ATAL YS I S, 3RD AMSTERDAM 1964111,163-83
ENG CA-64-278? G
BOREGK65SAO RPPESKOV GK SLIN'KH MG
SIMULATION AND OPTIMISATION OF CHF«ICAL RFACTPP.S
SPIT. CHFM. FNG. 1P( 3 I , 17(1-41 IQfci) FNG. C A-ft?-l ?7i-,6 C
PPRESKHV GK
OAVYDHVA
VM
COMPOSITION OF VANADIUM-SILICATES AS INVESTIGATED PY
bLtCTRON-PARAMAGNCT IC-RF SONANCF
DPKL. AKAD. NAUK SSS<» 1 71 ( •YALOVA NO SHASHKINA MF
PROMOTING ACTION OF'GROUP-I AND THE LANTHANIDE-GROUP
ELEMENTS ON VANADIUM CATALYSTS
. »NAOIEVYF KATAL IZATHRY OLYA KMNT _ .__
KISLOTY,NAUCHN.ISSLED.INST.UDnBR. I INSEKTOFUNG..SB.STATIE
VANADIEVYF KATALIZATDRY DLYA KMNTAKTN. PRUIZV.SERNOI
KISLOTY,NA ' '" '
1963.B5-9I CA-6^-?3e
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15
BROOM 48CSA HPHDSKV M BER'HJIN M
CONTACT SULFURIC-ACID DETERMINATION OF WATER FO<>MFD ON
THE CATALYST
HULL. SOC. CHIM. FRANCE 194B.470-2 CA-42-6495 G
BROKH t6STT 1ROKE *
SOLUTION TO THE S02 PROBLEM IN AIR PURIFICATION BY
OPERATIONAL AND INDUSTRIAL MEASURES
LF.FTVERUNREINIGUNGI 1966)36-4Z(GEPI CA-66-8H434 R
BROOEW66PMA BPOOMAN EW
HOAR TP
EVALUATION OF RELATIVE ACTIVITIES
PLATINUM METALS REV. 10( '"
PLATINUM METAL ALLOYS IN ELECTROCATALYSIS A FURTHER
- ACTIVITIES
l),135-9(1966)ENG CA-66-1086BO V
BRUSH 66DOA BRUSSET H LUOUET F
THE DESIGN OF A UNIT FOR THE SYNTHESIS OF SULF UR-TRIOX IDE
CHIM. INC., GENIE. CHIM. 9814).694-9119661FR. CA-6R-41608 B
BRUSH 66VCI BRUSSET H LUOUET F
VANADIUM CATALYSTS IN THE OXIDATION OF S02
CHIM.INO.,GENIE.CHIM.96(31,557-64.11966)F». CA-66-7260P U
BUDA 6MCO BUDAPEST I VEGYIMUVEK
IMPROVED CATALYST OF HIGH LOAD CAPACITY FOR SULFURIC-ACID
PRODUCTION
HUNG.152,893ICL. B 01JI.JUNE ?2,1966 CA-65-(P|-11835 F
HUKHSV65POA BUKHONETS SV
PRODUCTION OF A PLATINUM CATALYST
U.S.S.R. 105,486 (CL. B 01JI.DEC. 18,1965,APPL.OEC.19,1963
BUKUI 66IPA 8UKURADZHIEV I
INVESTIGATIONS OF POROUS ADSORBENTS AND CATALYSTS BY MEANS
OF DISTRIBUTIVE FUNCTIONS OF THE SURFACE WITH REGARD TO
ITS CURVATURE
IZV.!NST.OBSHTA.NEnRG.KHIM.,BULG.AKAD.NAIIK. ,4,103-131 1966)
BULG CA-66-119201 U
BULYII62NC>« BULYGIN II
NEW CONSTRUCTION MATERIALS FOR APPARATUS IN SULFURIC-ACI0
AND SELENIUM PRODUCTION
SB. MATERIALOV KONF. PO BOR'BES KORROZIE I.GORKI 1962 158-63
CA—61—373 B
BURKDB6BRST BURKHARDT DB
REMOVING SULFUR-TRIOXIOE FROM GAS MIXTURES
US 3,362.786 ( C. 23-175 I .JAN. 9, 1968.APPL. OCT.5,1968
CA—68 —(PI — 5 142 K
BURYKA63COA
BURYAK KA
COK
DNTAHINATIUN OF A VANADIUM CATALYST WITH CARBON-BLACK IN
SULFURIC-ACID PRODUCTION
TP. NAIICHN. INST. PO UDriHR . I INSRKTnFUNC. 1963,61-6
C4-61-330 E
CALCULATION OF THE RATE OF REACTION CONSTANTS IN THE
OXIDATION OF S02 TO S03 ON A VANADIUM CATALYST
ZH.PRIKL.KHIM. 36(91,1890-4(19631 CA-60-1147 C
BURYKA64PSA BURYAK KA AMEL IN AC
PREPARATION OF SULFURIC-ACID WITHOUT A CATALYST AT HIGH
VESTN. TEKHN. 1 EKON. INFORM. NAUCHN.-I SSLED. INST. TEKHN.
EKON. ISSLED.GOS.KOM. KHIM PROM. PR I GOSPLANE SSSR 1964(31
9-10IRUSSI CA-62-4938 G
BURYN163CFT BURYAK NI MARKOVA El
CATALYSTS FOR THE DIFFERENT STEPS IN THE OXIDATION OF
SULFUR-DIOXIDE
VANADIEVYE KATALIZATORY DL YA KONTAKTN PROI Z V. SERNOI KISLOTY
NAUCHN-ISSLED.INST.UDOBOR. I . I NSEK TOFUNG. , SB. STATE I 1963
62-7 CA-60-2372 B
BUTLJO60SPO BUTLER JD
SEMICONDUCTING PROPERTIES OF VANADI UM-PENTOXIDE AND THE
CATALYTIC OXIDATION OF SULFUR-DIOXIDE
TRANS. FARADAY SOC. 56,1842-50(1960) CA-55-15139 E
BUTYPY52ASO
ZHUR. FIZ.KHIM. 26. 692- 700( 19521 CA-47-5233 E
CABRC 66MST CABRILLAC C
METAL SPRAYING TESTS IN LABORATORY AND ON SITES
SOUDAGE TECH. CONNEXES 201 3-41 , 1 38-481 1 966) FR
,1 F
TARTARELLI R
CAGIS 67CPG CAGIANELLI S MOPELLI -
CATALYST POISONING AND GEOMETRY OF THE CATALYST PARTICLE
QUAD. IMG. CHIM. ITAL 3( 9) , 147-531 19671 I TAL CA-68-7271 5P
CALDPH52TMO CALDERBANK PH
THE MECHANISM OF THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
WITH A COMMERCIAL VANADIUM CATALYST A KINET1C•STUDY
J.APPL.CHEM. 2,489-92(1952) CA-48-8003 1
CALDPH53CPC CALDERBANK PH
CONTACT PROCESS CONVERTER DESIGN
CHEM.ENG. PROGR. 49,585-99(1953) CA-48-412 I
MANNING FS
THERMODYAMIC
CANJLN66TPN CANJAR LN JONES CR
THERMO PROPERTIES OF NON-HYDROCARBONS
PROPERTIES OF SULFUR-DIOXIDE
HYDROCARBON PROCESS.PETROL.REFINER 451 4),161-4(1966)ENG
CA-65-3089 E
CARBJ 67FOC CARBONELL J
FABRICATION OF CATALYSTS
AFINIOAO 24(2501,316-1711967ISPAN. CA-68-33587 D
177
178
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CARBJJ66TDP
CARHJJ67EAO
CARRS 62DOF
CATHJ 45ST
CHAGVT65UOM
CARBERRY JJ GORING RL
TIME-DEPENDANT PORE-MOUTH POISONING OF CATALYSTS
J.CATALYSIS 5(31,529-351 19661ENG CA-65-8056 H
CARBERRY JJ
ENGINEERING ASPECTS HP CATALYTIC REACTIONS
QUAD.ING.CHIH.ITAL.314),73-81(1967) .IT«L CA-67-15332 S
CARRA S STABILINI HP
DESIGN OF FIXED-BED TUBULAR CATALYTIC REACTORS
CHIM. IND.(MILAN) 44,851-4(1962) CA-58-113B D
CATHALA J '
SULFUR-TRIC
BRIT. 57i,207,AUG 13,1945
CA-41-(P)-841 0
CHAGUNAVA VT
USE OF MANGANESE CATALYSTS IN CHEMICAL INDUSTRY
ISSLEO.PO PRIMENENIYU MARGANTSEVYKH KONTAKTOV V KHIM.PROM
AKAO.NAUK GRUZ .SSR . INST.NEORGAN.KHI M. I ELECTROKH IM. 1165 RUSS
CA-65-4706 A
CHAIM 66PLH CHAIKIVSKY H
PREVENTION OF LOW AND HIGH-TEMPERATURE CORROSION AND
DEPOSITS IN OIL-FIRED STEAM BOILERS BY COMBUSTION
. WITH LOW AIR SURPLUS
SCHWEIZ. BL. HEIZUNG LUEFTUNG 33( 4) , 137-41 1 1 966 I GER
CA-66-58777 N .
CHAMJB66CPF CHAMOUX JP
COMPUTER PROGRAM FOR AN ADIABATIC CATALYTIC REACTOR
CHIM.IND., GENIE CHIM 951 A ) , 1389-92 I I96MFR CA-«.5-16521H
CHAMRP66LOD CHAMBERS RP ROUDART M
LACK OF DEPENDENCE OF CONVERSION ON FLOW PATE IN CATALYTIC
STUDIES
J. CATALYSIS 6( 1 1 , 1M-5I 1966IENG CA-65-12B95 D
CHAMHY36SOT CHANG HY CHANG TH
STUDIES OF THE RATE OF REACTION IN THE VANADIUM CONTACT
SULFURIC-ACIO PROCESS
J.CHEM.ENG.(CHINA)3,315-24(1936)CA-3l-3217-9
CHANMC59KSO CHANG MC KUO ST WANG SC
KINETIC STUDIES ON THE OXIDATION OF SULFUR-DIOXIDE ON
VANADIUM CATALYSTS Ml. A COMPARISON OF THE RATE EQUATIONS
OBTAINED WITH SOME INDUSTRIAL VANADIUM CATALYSTS
HI) A KUNG HSUCH PAP 1959, NO. 2, 98-1 01 CA-S7-16127 H
CHASJC66LOP CHASTON JC
LOSS OF PTQ2 FROM HEATED PT
MECHANISM
DLATINUM METAIS
A BOUNDARY LAYFR DIFFUSION
9i-3( 19&MENG CA-65-14452 F
CHEM 64POS CHEMICAL CONSTRUCTION CORP.
PRODUCTION OF SUIFUR-TRIOXIOF
BRIT. 961,904 (CL.C P1B),JUNE 24 , 1 964, IIS. APPL. SE PT. 1R.1961
CA-6l-(P)-919Q E
CHE1* 64UAS CHEMIEBAU
UTILIZATION OF AMMONIUM-SULFITF SOLUTIONS FROM THE FINAL GAS
SCRUBBING SOLUTION OF THE CONTACT SULFUR IC-AC11)
INSTALLATIONS
CHEMIEBAU OR.A ZIEREN GMRH NETH. APPL.6,507,567 BKINA El OFRYUZHKINA VI
THE IGNITION TEMPERATURE OF A WFAR RESISTANT VANADIUM
CATALYST FOR THF OXIDATION OF SULFUR-DIOXIDE
KHI.M PROM. 1965(2), I 1 5-1 61 RUSS >CA-6?-l 421 4 C
CHF.SVS52SCA CHESLOVA VS BORFSKTV GK
SPECIFIC CATALYTIC ACTIVITY PF METALLIC PLATINUM
OQKLAOY AKAD.WAUK S.S.S.R. 85, 177-a( 1952) CA-46-99M C
CHESVS56TSC CHFSLOVA VS BORESKOV f.K
THE SPECIFIC CATALYTIC ACTIVITY OF METALS SULFUR-DIOXIDE
OXIDATION ON PLATINUM CATALYSTS
ZHUR.FIJI.KHIM. 1p,?SfrO-7l I95h) C.A-5I-9276 f
179
180
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/27/69
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19
CHMUD 65AOC CHMURNY 0
AUTONATION OF CONTACT REACTORS IN THE CHEMICAL INDUSTRY
AUTOMAT I ZACE ( PRAGUE ISC 61 , 144-91 1965) ( SLOICA-64-307 C
CHOUA 67SCP CHOU A RAY WH ARIS R
SIMPLE CONTROL POLICIES FOR REACTORS WITH CATALYST DECAY
CHOUA 67STO CHOU A
SOME TOPICS IN OPTIMIZATION OF REACTORS WITH CATALYST
DEACTIVATION
- HI"OF,LMS,ANN
CHRIA 68AEC CHRISTENSEN A
APPARATUS FOR EXOTHERMIC CATALYTIC REACTIONS
U.S. 3,366,460 (CL. 23-289), JAN. 30 ,1968 , APPL. MARCH 11,1964
CA-68-IP 1-79887 E
CHRICN65GSB CHRISTY CM
GRADED SUPPORT BED FOR CATALYSTS
67,APPL.MARCH 28
CHRIDW66STM
CHUFGI34EOA
U.S. 3,311,686 (CL. 264-117).MARCH 28,1967,A
1967,APPL. MARCH 15,1965 CA-66-(P)-107939 C
CHRISTOFFERSON DM
STEEL TANK MAINTENANCE
WATER WASTES ENG 413).52-5(1967IENG CA-66-98403 U
CHUFAROV GI
K( ---
AGAFONOV NN
TATIEVSKAYA ED
^C
CHUNKY66SIP CHUNG KY
.ULPINA Kl
FFECT OF A POROUS SILICA-GEL CATALYST CARRIER ON THE
VELOCITY OF OXIDATION OF SULFyR-pIOX! DE GAS
DAEHAN HHAHAK HHOEJEE 1012 I,76-9011966)KOREAN CA-67-66087Y
CIBOS 65PFN CIBOROMSKI S
PROSPECTS FOR NUCLEAR RADIATION APPLICATION IN CATALYSIS
WIADOMOSCI CHEM.19l7t,51I-21(1965)POL CA-63-17189 0
CIBOS 67CNR CIBOROWSKI S
PROSPECTS FOR NUCLEAR RADIATION APPLICATION IN CATALYSIS
WIADOMOSCI CHEM. 1O|7 I.511-21(19651 POL CA-63-17189 0
CIGDM 64SPC CIGDEMOGLU M
SOME PROBLEMS CONCERNING SULFURIC-ACID PRODUCTION
DEMIR VE CELIK I3(8),180-4(1964)TURKISH
CIMAJ 67POS CIMAOEVILLA J
PRODUCTION OF SULFUR IC-AC ID BY THE CONTACT PROCESS
FR. 1,489,906 ICL. C OIRI.JULY 2 R, 1 967,APPL. JULY 13,1966
LARCB25STF
LARCB27EGR
LEHJL66MOR
LUZJ 65FAR
SULFUR-TRIOXIDE FROM SULFUR-DIOXIDE
U.S. I,789,460,JAN. 20 CA-25-(P)-1344-l
PL ARK CH ™ "
EXOTHERMIC GAS REACTION SUCH AS OXIDIZING SULFUR-DIOXIDE TO
TRIOX1DE
US. 1.883,
570,OCT.18 CA-27-IPI-1C65-4
MAGNESIUM-OXIDE RECOVERY SYSTEM DESIGN ANP PERFORMANCE
TAPPI 49(81,127A-134AI1966IENG. CA-65-13263 F
CLUZEL J
FIXATION AND RECOVERY AS AMMONIUM-SULFATE
DIOXIDEIN INDUSTRIAL EFFLUENT GAS
OF WASTE
OFFICE NATIONAL INDUSTRIEL DE L'AZOTE. FR. 1,388,690 (CL.C
018 C, F 23Jt,FEB.16,1965,APPL.APRIL 29,1963 CA-63-1PI-3930C
OECOT J
LIENARO G
OEKP 63CUI COEKELBERGS R CRUEO A
DEGOLS L FRENNET A
TIMHFRM ANN I
CATALYSIS UNDER IRRADIATION IN THE PRESENCE OF NONMETALLIC
I NO."" USES LARGE RADIATION SOURCES.PRPC.CONF.,SALZBURG
AUSTRIA,1963 2 3-21 CA-61-2519 B
OLER 60ASD
ONNr,C2BCMS
ONNJF67RSP
C1RBPF52ROS
ORRTE67WDC
OTTWJ49EDA
OUGOR6STRO
COLE R SHULMAN HL
ABSORBING SULFUR-DIOXIDE ON DRY ION-EXCHANGE ROSINS
IND. ENG. CHEM. 52.859-60(1960) CA-55-5807 E
CATALYTICGHASSES SUCH AS THOSE SUITABLE FOR OXIDIZING
SULFUR-DIOXIDE TO TRIOXIDE
US. 1,935,177.NOV.14 CA-28-IPI-B67-B
CONNOLLY JF FLANNERY RJ MEYERS BL
RECRYSTALLIZATION OF SUPPORTED PLATINUM
J. ELECTROCHEM. SOC.114(3).241-3C1967)ENG CA-66-101063 R
CORBETT PF LITTLEJOHN RF
REMOVAL OF SULFUR-OXIDES FROM THE GASES
?ULL.BRIT.COAL UTILIZATION RESEARCH ASSOC.16,437-44(1952)
A-48-8517 H
CORRIGAN TE LEWIS WE " MCKELVEY KN
WHAT DO CHEMICAL REACTORS COST IN TERMS OF VOLUME
CHEM ENG. (N.Y.I 74(111,214-15 (19671ENG CA-6T-34237 - F
ELECTRIC DISCHARGE APPARATUS FOR THE SYNTHESIS OF
NITRIC-OXIDE FROM ATMOSPHERIC NITROGEN
US. 2,468, 173-4-5-7, APR.26, 1949 US.2,468,176 C A-43-1 P>-6096G
fK&SV SD2 A-NDUo1 ^N AQUEOUS SOLUTIONS ON MNS04
IND.ENG.CHEM.FUNDAMENTALS 4( 11 ,<•!-&( 1965) ENG C A-62-5931 F
181
1C2
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COIICPW67HTA
REACTION IN A CATALYST PORE
A.I.CH.E. J. 13(5). 1031-31 1967IENG CA-68-14430 F
CHEMICAL
COURP 65IES COURVOISIER P MAURETTE E RAVOIRE J
ISOTOPE EFFECT OF SULFUR DURING THE OXIDATION OF
S02 IN SULFURIC-ACID AND THE MECHANISM OF THIS
^' 62<2),219-21(1965)FR. CA-62-14169 E
CPAXSR52RSF CRAXFORD SR POLL A WALKER MJ
RECOVERY OF SULFUR FROM FLUE-GAS BY THE USE OF AMMONIA
J.INST.FUEL,25,13-14(1952 I. CA-46-22670
CRAXSR66APF CRAXFORD SR
AIR POLLUTION FROM POWER STATIONS
BER. INT. VORTRAGSTAG
PRO AQUA BASEL,1965 77-921 PUB.1966) CA-67-76101 N
CULLCF66TKO CULLIS CF HENSON RM TRIMM DL
THE KINETICS OF THE HOMOGENEOUS GASEOUS OXIDATION OF
SULFUR-DIOXIDE
PROC.ROY.SOC.ILONDON),SER. A295I1440),72-83119661ENG
CA-65-1776 F
CYBUA 67M1C CYBULSKI A GROMAnOHSKI J
MATHEMATICAL MODEL OF CATALYTIC REACTORS
DAVIL 62ASD DAVIGNON L
ACTION OF SULFUR-DIOXIDE ON TITANIUM ZIRCONIUM HAFNIUM
VANADIUM NIOBIUM AND TANTALUM
COMPT. REND., SER. C 262(181,1360-2(1962) CA-65-3296 E
DAVIP 59CFO DAVIES P
CATALYSTS FOR OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIOXIDE
BRIT. 808,150,JAN 28,1959 CA-53-(P)-l1781 C
DAVIP 63ST DAVIES P
SULFUR-TRIOXIDE
BRIT. 756,683,SEPT. 5,1963 CA-51- I Pt-8396 D
DAVTOK58PEI OAVTYAN OK OVCHINNIKOVA EN
THE PROBLEM OF EXPERIMENTAL INVESTIGATION OF SEPARATE STAGES
OF HETEROGENEOUS CATALYTIC PROCESSES
SOVESHCH. PO KATALIZU 1956,NO.1,414-18,PT.1(PUB.19621
CA-59-67 C
OAVTOK61ETR DAVTYAN OK
MANAKIN RA
MISYUK EG
EFFECT OF TEMPERATURE ON THE RATE OF FORMATION OF SULFURIC
-F SULFUR-DIOXIDE ON ACTIVATED CARBON BY
TUSZYNSKI
GENER
PRZEM.CHEM. 4615»,244-611967IPOL CA-67-45563 K
GROMADOUSKI
AL PRINCIPLES
BY THE OXIDATION 0 ...
THE LIQUID CONTACT METHOD
NAUCH. EZHEGODNIK ODESSK. GOSUDARST
NO. 2,113-15 CA-56-16963 E
EN
UNIV.,KHIM.FAK. 1961
CYBUA 67MMQ CYBULSKI A GROMADOUSKI J
MATHEMATICAL MODELS OF CATALYTIC REACTORS
PRZEM. CHEM.46(61.308-1411967IPOL CA-67-92207 G
DAMKG 43ETI UAMKOHLER G
EXCESS TEMPERATURE IN CATALYST GRAINS
Z.PHYSIK. CHEM. 193.16-28(1943) CA-39-2689-3
HEAT AND MASS
DARHK 66CFG DARBY K
HEINRICH DO
CONDITIONING OF FLUE-GASES IN BOILER PLANTS FOR IMPROVEMENT
OF DEGREE OF SEPARATION OF ELECTROSTATIC FILTERS
STAUB REINHALTUNG LUFT 261 1 1 I , 464-81 1966> GER CA-66-67753 0
OAVIB 64KCO DAVIDSON B THODDS G
KINETICS OF THE CATALYTIC OXIDATION OF SULFUR-ni OXIDE
A.I.CH.E. J. 10(4), 568-731 1964) CA-61-8942 A
DAVTOK61IMO DAVTAN OK _..
INVESTIGATION OF THE MECHANISM OF OXIDATION HYDROGENATION
AND ELECTROCHEMICAL COMBUSTION ON SOLID CATALYSTS
OXIDATION OF SULFUR DIOXIDE ON ACTIVATED CARBON AT 20-DEG
IN THE PRESENCE OF WATER VAPOR
ZHUR. FIZ. KHIM. 35.713-18 (1961) CA-55-17163 0
DAVTOK61MOH DAVTYAN OK TKACH YA
MECHANISM OF OXIDATION HVDROGENATION AND ELECTROCHEMICAL
COMBUSTION ON SOLID CATALYSTS CATALYTIC PECULIARITIES
OF SURFACE OXIDES ON CARBON
ZHUR.FIZ.KHIH. 35.992-8(19611 CA-56-48 F
DAVTOK6ITCA DAVTAN OK OVCHINNIKOVA EA GRIGOR'EVA GA
THE CATALYTIC ACTIVITY OF PLATINIZED NICKEL IN THE OXIDATION
OF SULFUR-DIOXIDE
NAUCHN. EZHEGODNIK.OOESSK.cos.UNIV.,KHiM.FAK.i96i
MANAKIN BA
MISYUK EG
OAV.8 64KOT DAVIDSON
OX,OATION nF Sl)LFUR.DI Mloe
RELATION
nAVIBH67TCP DAVIS BW
PICE OK
THERMDYNAMICS OF THE CRITICAL POINT LIQUID-VAPOR SYSTEMS
J.CHEM.PHYS. 47( 12) . 5043-5311 <^7 )TNG CA-6B-81897 8
OAVTOK61TMO DAVTAN OK
POLISVUK VN
THE MECHANISMS OF OXIDATION HVDROGENATION AND
ELECTROCHEMICAL COMBUSTION ON SOLID CATALYST
BETWEEN DEPOLARIZING OXIDES ADSORBED ON CARBON AND
PLATINUM AND THE CATALYTIC ACTIVITY IN THE OXIDATION OF
SULFUR-DIOXIDE
ZHUR.FIZ.KHIM.35. 1186-9K 19611 CA-56-5438 H
DEGO 5600T DE GOBA IN.CHAUNY C CIREY
DETERMINATION OF THE DEGREE OF OXIDATION OF SULFUR-DIOXIDE
IN THE MANUFACTURE OF SULFURIC-ACID
BRIT. 759.056,OCT.10,1956 CA-51-(P)-9105 H
1C3
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nEGTIPfi6°l)S OEGTYAREV IP
PRODUCTION OF SULFUR IC-AC II) FROM FLUE-GAS FROM OIL TREATMENT
NCFTEPERERAB NEFTF.KHIM. 19661 U I , 20-41 RUSS) CA-66-67396 0
DEPKJ 64MUT
DERKJ 64TIJT
SEHNDUTKA J
MANUFACTURING UP TO &n PER CENT OLFUM OR SULFIIRIC-ACID
CZECH. 111,646(CL. C 013 I,AUG.15,1964,APPL.JUNE 16,1962
CA-62-1P)-4941 B
POPPEL f.
FELDMAN 0
OIACV 55POV UIACONF.SCU V
CCRLATEANU E
PREPARATION OF VANADIUM-BASE CATALYSTS FOR THE SULFURIC-AC ID
INDUSTRY
BUL.INST.POLITEH,IASI l.NO.1-2,53-66t1955 I CA-51-12445 I
DMID 6-5TRO OlflTROV 0 BUYUKLIEV G
THE RECOVERY OF H2S04 FROM WASTE GASES
RUOnOOBIV MET. (SOFIA) 20(9l.22-5.2B22-4(1966)RUSS CA-66-69286 C
OONOJR67SAP OCNOVAN JR STUBER PJ
SULFURIC-ACIO PROOUCTION FROM ORE ROASTER GASES
J.METALS 191 ID,, 45-5Pi 1967IENG CA-68-14548 A
OOROAG17CEC OCBOSHEVSIIU AG PAVLOV GS
THE CONTACT EFFECT OF CHARCOAL IN PXIDATIVE REACTIONS
J.RUSS.PHVS.CHEM.SOC. 22,(7),963-77(1967)ENG CA-67-55630 U
DUPARC L HENGER 0 URFER CH
GASEOUS CATALYSIS BY METALS OF THE PLATINUM GROUP
HELVETIA CHIM. ACTA 8,600-31(19251 CA-20-5-9
HORN FJN
JACKSON R
DYSON DO
SCHLESINGER CB
REACTOR OPTIMIZATION PROBLEMS FOR REVERSIBLE EXOTHERMIC
REACTIONS
CAN. J. CHEM.ENG.4515),310-181I967)ENG. CA-68-41615 B
RORESKOV GK
KASATKINA LA
DZISAP61TEO OZISYAK AP
KOCHURIKHIN VE
THE EFFECT OF ALKALI METAL SULF'vTES ON THE CATALYTIC
. PROPERTIES OF VANADIUM
KIN ET IK A I KATALIZ 2,727-31(1961) CA-56-9968 C
DZISVA64RBP DZIS*KO VA
RATIONAL BASIS FOR PREPARING CATALYSTS
NAUCHN. OSNOVY PODBORA I PROIZV. KATALIZAIOROV,AKAD.NAUK
SSSR.SIBIRSK.OTD. 1964 , 75- 34(RUSS)CA-63-4987 A
DZISVA64SAO OZIS'KO VA
SPECIFIC ACTIVITY OF OXIDE CATALYSTS
NAUCHN. OSNOVV PODBORA I PRO1ZV. KATALIZATOROV,AKAD.NAUK
SSSR, SIBIRSK.OTO. 1964,85-95 RUSS CA-61-4986 E
IBS
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EDMIWC67AHH EDMISTER HC
APPLIEIJ HYDROCARBON THERMODYNAMICS HEAT CAPACITY DIFFERENCES
HYDROCARBON PROCESS 46(61.187-92t19671ENG CA-67-57742 F
EOMIWC67AHT EDMISTER WC
APPLIED HYDROCARBON THERMODYNAMICS
FPIFVS66EHV EPIFANOV VS
IDEAL GAS STATE
PROPERTIES
HYDROCARBON PROCESS 46(3 I, 119-23(1967 IENG CA-67-110256 D
EDSTJ067SDC EDSTROM JO LOFBLAD B
STEELS FOR DIFFICULT CORROSION CASES IN THE CHEMICAL
INDUSTRY
WERKST. KORROS. 18<9 I,769-7711967)GER CA-67-102246 K
EHREH 66FMR EHRENBERG M
' - - FILTER "MASS FOR THE REMOVAL OF SULFUR-DIOXIDE FROM WASTE
GASES
CHEM. INGRt-TFCH. 3817)(I966IGER. CA-65-14877 C
EKLURB57TRO EKLUND RB
THE RATE OF OXIDATION OF SULFUR-DIOXIDE WITH A COMMERCIAL
VANADIUM CATALYST
STOCKHOLM ALMOVIST & HIKSELL 1957 CA-51-6100 B
ELENO 66ASO ELFNKOV 0
KRUSTEV I
_ BDYADZHIEV K .
ON THE ABSORPTION OF SULFUR-DIOXIDF BY SODIUM-CARBONATE
SOLUTION IN A VENTURI ABSORBER
IZV. INST. OBSHTA NEORG. KHIM..BULG. AKAD. NAUK. 4,153-66
(1966IBULG CA-66-67332 R
ELEND A6HMT ELENKOV D BOYADZHIEV K
HYDRODYNAMICS AND MASS TRANSFER IN A NOZZLELESS VENTURI
ABSORBER ABSORPTION OF SULFUR-DIOXIDE INTO WATER
AND WATER SOLUTIONS OF SURFACE ACTIVE AGENTS
IZV. INST. OBSHTA. NEORG. KHIM. RULG. AKAD. NAUK.4,167-72
(1966IBULG. CA-66-67333S
ELEYDD67AIC
ELLIC 17MSA ELLIS_C
EMPR 62ROS
ELEY DD PINFS H HEISZ PR
ADVANCES IN CATALYSIS
ACADEMIC NEW YORK 1967 CA-68-31&7R J
. .. ._ KUNIN TI
FFECT OF WATER VAPORS ON THE REACTION OF SODA WITH
MAKING SULFUR IC-ANHYDR IDE
CAN., 177,1*5,MAY 22,1917 CA-12-(PI-83-7
EMPRESSA AUXILIAP OE LA INDUSTRIA S.A.
RECOVERY OF SULFUR-OIOXIDF FROM INDUSTRIAL GASES
FR. 1,356,116 (CL. C Q10IMAR. 2? , 1 964. SPAN. APPL MAY.3,196?
CA-62-(P)-2525 A
1C.
T AND HCA1FM
SULFUR-DIOX...
IZV, VYSSH. UCHEB, tnvc
19661RUSS) CA-66-7997 Z
AT TEMPERATURES ABOVE 100-DEGREES
ZAVED.,KHIM.KHIM.TFKHNOL.9(5),785-99
EREMVY38IOC EREMENKO VY SATSUK AF
INFLUENCE OF CARBON-MONOXIDE ON THF ACTIVITY OF PLATINUM
CATALYSTS DURING THE OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE
IZVEST.NOVOCHERKASSKOKO IND. INST.,KHIM.CHAST 3,30-43(1938)
KHIM.REFERAT.ZHUR.l,N0.11-12,63-4( 1938) CA-33-8934-5
ERICH 67TSC ERICKSON H RUSSELL HG
TRANSFERING A SLURRY OF CATALYST TO A REGENERATION ZONE
U.S. 3.295,897 (CL. 302-66),JAN. 3,1967,APPL.FER 27,1964
CA-66-(P)-77779 F
LAKHMOSTOV VS
SUKHAREV GA
ENGE 65CCIM ENGELHARD INDUSTRIES IN
CATALYTIC OXIDATION UNI
BRIT. 997,611 (CL. B OU),JUIY 7,1'Jfr* US APPL. SEPT.4,196?
CA-63-|P)-112?t C
ERMAA 68AMQ FRMAKOVA A
SMIRNOV NP
AERODYNAMIC MODELLING OF CONTACT APPARATUS MODELLING OF A
REACTOR FOR THE OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE
VSES.KQNF.KHIM. REAKTORAM 3,570-8<»USSI CA-68-70489 U
ESELIM640CI ESELEV IM ' MUKHLENOV IP TRABER DG
OPERATIONAL CONDITIONS IN THE COMBINED CONTACT-CHAMBER
PROCESS
ZH.PRIKL. KHIM.37(6),1204-1011964) CA-61-11643 E
ESELM64UOA ESELEV IM MUKHLENOV IP TRABER OG
USE OF AN IRON CATALYST IN THF CONTACT CHAMBER PROCESS
ZH. PRIKL. KHIM. 37(41,722-7(19641 CA-61-2522-D
ESSO 64IMT ESSO RESEARCH AND ENGINEERING CO.
IMPROVEMENT OF THE MASS TRANSFER FROM A GAS TO A POROUS
CATALYST OR ADSORBENT BY PRESSURE OSCILLATIONS
NETH. APPL. 6,505,351 (CL. B 01J),OCT 29,1965 U. S. APPL. APR IL
28.1964 CA-64-IPI-13794 F
ESSO 66FDM ESSO RESEARCH AND ENGINEERING CO.(BY JOHN S. BOTZOLD)
FINELY DIVIDED METALLIC CATALYSTS
FR. 1,438.140 (CL. B 01JI.MAY 6,1966 U.S.APPL JULY 6,AND
SEPT. 25,1964 CA-66-1 P )-1443CB
ETOCP 66MTS ETOC P
MODERN TECHNIQUES OF STUDY OF CORROSION AND ATMOSPHERIC
POLLUTION APPLIED TO BOILERS AND FURNACES
IND. CERAM NO. 5B4,328-33 DISCUSSION 333-5U96MFR
CA-65-691H D
ETRIJJ29SHG ETRIDGE JJ
STANNIC-HYDROXIDE GEL
RPIT. ?33,670,JUNE 5,1929 CA-2*-tP)-565-3
107
138
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I64ASA EZHKOVA ZI lOFFf II KAZANSKM VB
KRYLOVA AV LYUB4RSKII AC HARGOLIS LY
ACTIVITY STRUCTURE AND ELECTPICAL PROPERTIES OF MIXED
VANADIUM CATALYSTS
KINETIKA I KATALIZ 51 5 1, 86 1-71 1 964 ) RUSS.
FAHITZ66DOA FAHIDY TZ PERLMUTTER DP
DYNAMICS OF A SURFACE-CATALYZED CHEMICAL SYSTEM
CAN.J CHEM.ENG.44121,95-9119661ENG CA-65-4707 D
FAPR 30AFA FARBEWIND A.-G.
APPARATUS FOR AFFECTING GAS REACTIONS BY MEANS OF ELECTRICAL
DISCHARGES
BRIT. 354, 735, FEB. 5,
CA-26- I » ) -3704-3
FAPRWERKE HOECHST A.-G.
CONTACT MASSES FOR HETEROGENEOUS GAS CATALYSIS
GER. 953,603 DEC. 6, 1 956ICL . 12G, 1) CA-52- ( PI -1 8963 H
FAR9 56CMF
FARB 62VC
FARB 64STP FARBENFABRIKEN BAYER A.G.
FARBENFABRIKEN BAYER A.G.
VANADIUM CATALYST
BRIT. 898,985 ,JUNE 20,196?
CA-57-(P)-6670 0
SULFUR-TRIOXIOE.PROCESS.
FAR3IG35CGR
FEOOAV67COT
1,181,181 ICL.C fHB)NOV.12,1964 APPL. APR. 15 ,1961
CA-62-(P)-3695-C
FARBENINO 1C
CATALYTIC GAS REACTIONS
FR.790,529,NOV.22,1935 CA-30-(P1-3119-7
FEDOTOV AV BESKOV VS SLIN'KO MG
CONTROL OF TEMPERATURE BY ADMISSION OF A COLD COMPONENT AS A
MEANS FOR ENSURING OPTIMAL CONDITIONS FOR AN EXOTHERMIC
REACTION
KINET.KATAL .81 l),198-202( 1967)RUSS CA-66-106383 E
FEOONP65EOT FEDORENKO NP
_ . . LIPKINA SO
ECONOMICS OF THE PRODUCTION OF
SULFUHIC-ACID FROM WASTE
SULFUR CONTAINING GASES
KHIM PROM. MI 81,597-91 1965)RUSS CA-64-323 A
FERRG 661FI FEKKtlHLO G REVERSES! A
INSTALLATIONS FOR INDUSTRIAL GAS CLEANING PROCESS
OPTIMIZATION FOR OPERATING MULTIPLE INSTALLATIONS IN ANY
REGIME
INGEGNERE (MILAN) 40110?),897-904 119661 ITAL. CA-66-57363 N
FF.RRG STEIP FFRRAIOLO r. REVERBERI A
EFFECT OF IRREGULAR PORES ON THF SFLFM1VITY OF A POROUS
CATALYSTS
ANN. CHlM.RdMC 57< 5) . 5B8- 94( 1967 11 T Al CA-67-85344 X
FFR3C, 67EPG FERRAIOLO G REVFR8ERI A
EFFECT OF PORE GEOMETRY ON THF ACTIVMY AND AGING OF
CATALYSTS
ANN.CHIM.IROMF 157(41 ,450>6l( 19»:71I TAI CA-67-94344 Y
FIALRM60DDT FIALKO GM
DETERMINATION OF THE RATE OF CONVERSION OF SULFUR-DIOXIDE
INTO SULFUR-TRIOXIOe
USSR. 152, 625,OCT.20, I960 CA-5S-IPI-12794 B
FILAVH66TOT FILATOV VU MUKHLENOV IP TRABER DG
RARTOV AT
TESTING OF THE APPARATUS FOR THE OXIDATION OF CONCENTRATED
SULFUR-DIOXIDE
ZHUR.PRIKL.KH1M. 3914 1,780-41 I 966)RUSS CA-65-323 C
FILIGC.66POS FILIPPOV GG VOL IN YM SADOVSKI I AS
CHESNOKOV 6R SAKOOrNSKII KI
CARRYING OUT OF HETEROGENEOUS CATALYTIC REACTIONS
USSR. 197,520 (CL.R OUI.JUNE 9,1967,APPL.FEB. 24 , 1966
CA-68-(P)-8R608 S
FISCHC64PCR FISCHER HC
POROUS CERAMIC BALLS F0<» CARRYING CATALYSTS
U.S. 3,145,183 (CL. 252-477),AUG.18,1964,APPL.DFC.16,195B
CA-61-(P)-10429 F
F1SCS 65ATD
FISCHER
ALLOWANCE
FOR THE TtMPERATURE DEPENDENCE OF SPECIFIC HEAT
OF INDIVIDUAL GASES AND GAS MIXTURES IN THER100YNAMIC
CALCULATION FOR GAS FLOW MACHINE
FKEIBERGER FOP SCHUNSH. , A 381,117 C I 965 IGER.CA-65-96 F
FISCS 66TTS FISCHER S
THE T-S/R AND I-S/R DIAGKAMS FOP IDEAL-GASES
WISS. Z TECH. UNIV. DRESDEN. 1 51 4 ), 71 3- 191 1 9661 GER
CA-67-47796 N
FIVE 66ROS FIVESPENHOET
RECOVERY OF SULFUR FPOM INDUSTRIAL GASES
FP. 1,450,441 ICL C 01U. C 10J .. AUG. 26. 1966, APPL .DEC. 29, 1964
CA-66-(P)-87178 Y
FLIND 5 1 COO FLINT D LINDSAY AW
CATAIYTIC OXIDATION OF SULFUR-DIOXIDE ON HEATED QUARTZ
SURFACES
FUEL 31,288(1951) CA-46-7C7 H
F(JSrRM66ACM FOSTER RN BUTT J8
A COMPUTATIONAL MODEL FOR THE STRUCTURE OF POROUS MATERIALS
EMPLOYED IN CATALYSIS
A.I.CH.E. J. 12( 1),1RO-S( 19661FNG CA-fc^-llllJ A
FOUL A 55CCO
FRANM 64PSD
FOULON A
CATALYTIC COMRUSTION OF GASEOUS IMPURITIES IN HASTF AIP
OEL-GASFEUERUNG 1T( 4 1 , 462- 51 I 955 IGER CA-63-4858 fi
FPAN7 M KLIUECEK R
PROCESSING SULFllR-OIflXIDF FROM T OM8 US T I QN OASFS
CZtCH. 11?, 995, MAY 15,1964 APPL. JULY 22,1961
CA-61-1 PJ-^Z^SD
190
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PAGE
FRANTT65RDS FPANKENBERG TT
REMOVAL OF SULFUR FROM PRODUCTS OF COMBUSTION
"ROC. AM. PETROL. INST..SECT. Ill 45(31,365-70 (1965IENG
CA-66-495B3 U
FRAZJC290C
FRAZJH40ANM
FROMGF66HAM
FRUHAN4CCOH
GABRCQ47CCT
FRAZER JCN
OXIDIZING CATALYST
U.S.Ii602,404,OCT.12
CA-20-(P)-378ft-2
FRAZER JH KIRKPATRICK WJ
A NEW MECHANISM FOR THE ACTION OF THE VANADIUM-PENTOXIDE
SILICA-ALKALI PYROSULFATE CATALYST FOR THE OXIDATION
OF SULFUR-DIOXIDE
J.AM.CHEM.SOC. 62.1659-60(1940) CA-34-6156-6
FROMENT GF
HEAT AND MASS TRANSFER IN CATALYTIC BEDS
GENIE CHIM. 951 21,41-531 1966)FR. CA-65-1BOO R
FRUMKIN AN
CONFERENCE HN HETEROGENEOUS CATALYSIS
J. PHY S.C HEM. I U.S. S.R.I 14, 1151-1379(19401
GABRIEL SON CO
CALCULATION OF THE OVERHEATING OF CATALYST PARTICLES IN THE
OXIDATION OF SULFUR-DIOXIDE
TEK.TID. 77,859-62(19471 CA-42-3918 0
GAFJAA650CG GAFUROV AA
OPTIMUM CONTROL OF SUL F'.lRIC-AC ID PRODUCTION WITH THE AID
OF COMPUTERS
VOPR. VYCHISL. MAT. I TEKHN.,SB 1965{8 I,95-109(RUSS)
CA-65-18203 H
GALESF67RAR GALEANO SF
REMOVAL AND RECOVERY OF SULFUR-DIOXIDE IN THE PULP MILL
INDUSTRY
DISS.ABSTR. B 27(101,354911967IENG UNI V.MICROFILMS(ANN ARBO
R.MICHt,ORDER NO.67-3472,254PP CA-67-83103 T
GALESF67SDR GALEANO SF
SULFUR-DIOXIDE REMOVAL AND RECOVERY FROM PULP MILL POWER
PLANTS
J. AIR POLLUT. CONTR. ASS.
CA-68-1S839 H
HARDING CI
RECC
17(8).536-9I1967IENG.
GANZSN65DUF
GANZ SN KUZNFTSOV IE
DESIGN OF UNIFORM-FLOW TOWERS WITH CENTRIFUGAL ATOMIZERS
.... - IEHN. ZAVEOEN --
CA-63-2637 E
IZV. VYSSHIKH UCHEBN. ZAVEOENII.KHIM. I KHIM. TEKHNOL.8(1)
151-4(1965)RUSS "- ' '
GANZSN65SOR GANZ SN KUZNETSOV IE PPHGAIKO VV
SULFUR-PinxinF REMOVAL FRO" GASES Tn HRTMN AMMONIIIN-SULFATF
KHM. TFKHNOL., RESP. IEZHVEdflMSTV. NAUCHN.-TEKHN. SR.
1 = 65(2) 47-521 RUSS) CA-65-140'J6C
GANZSN66PNE
GARBC 4800S
GARTFE66COA
GANZ SN
PUR IF 1C
KUZNETSnv IE
CATION OF NITROSE EXHAUST GASES
U.S.S.R. 184,811 (CL. B 010),JULY 30.1 966, APPL . MARCH 22
1965 CA-66-(P)-68701 X
GARBATO C
OXIDATION OF SULFUR-DIOXIDE
ITAL.435.452.MAY 18,1948 CA-44-(P1-2716 A
GARTRELL FE
CONTROL OF AIR POLLUTION FROM LARGE THERMAL POWER STATIONS
REV. SOC. ROY. BELGE ING. I NO NO. 11,471-82(1966)ENG
CA-66-58626 N
GEIBEV56TPO GEIBHVICH EV
THF PROCESS Of THE OXIDATION OF SULFUR-DIOXIDE WITH
VANADIUM CATALYSTS
GtTEPOGENNYI KATALIZ V KHIM. PROM SRORNIK 1955 396-fl REFERAT
ZHUR.KHIM.1956 CA-52-lM"7-B
GEIBEV56TRF GEIBOVICH EV BORESKOV GK
TEMPERATURE RELATION FOR THE PATE OF OXIO&TION OF
SULFUR-DIOXIDE ON VANADIUM CATALYSTS
ZHUR,FIZ.KHIM. 30.1801-611956) CA-51-7818 F
GEISE 65SP.S GEISLER E
SEPARATIOI ....
GER. 1.191,793 (CL. C 01B)
CA-63-(P)-67129
SEPARATION AND RECOVERY PF SULFUR-DIOXIDE FROM WASTE GASES
___ . .-. ... - .APRIL 29,1965,APPL. DEC. -~
17,1963
GELEH 66MAH
GEMER 65SSD
GENF 67CFC
GERBFV63EOP
GFLENSOY H
MATERIAL AND HEATING BALANCE CALCULATIONS IN CHEMICAL
TECHNOLOGY
KIM. MUHENDISLIGI 19, 35-47 I 1966) ( T(IRK) C A-65-1 81 76-B
GEMERDONK R
SCRUBBING OF SULFUP-DIOXIDE FROM FLUE-GASES
CHFM. INGR.-TECH. 37(11),1136-911965IGER. CA-64-3084 A
GENERAL AMERICAN TRANSPORTATION CORP.
CATALYSTS FOR COMPLETE OXIDATION WITHOUT FLAME ANP THFIR
PROCESS OF PREPARATIHN
FP. 1,466,195 ICL.B 01J.F 24Ct.JAN.13,1967,APPL.JAN.31,1966
CA-67-IP1-6R019 B
GFRBMRT EV BOGATYREVA VM
FFFECT OF POTASSIUM-OXIDE ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE OXIDATION OF SULFUR-DIOXIDE AT LOW
TEMPERATURES
VANADIEVYE KATALIZATORY HLYA KPNTAKTN.PROIZV.SERNOI KISLOTY
NAUCHN-1SSLEO.INST. UOORR I INSFKTOFUNG.,SB.STATEI 1°63
43-7 CA-60-3527 0
GFRBEV63EOS GERBURT EV
GR IGOR'EVA AS
EFFECT OF S IL I CON-TE TRAFLOURIOF ON A VANADIUM CATALYST
KATALIZATORY 1)1. YA CONTAK TN. PROI ZV. SERNOI KISLOTY
VAN1DIFVY .
NAUCHN-ISSLEO.INST.Unrmni*. | INSFRTOFUNG.SB.STATEI
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150-8
1S1
192
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VASIL'EV BT
GH'REVt3SFC GFRSURT EV GLEIKHENGA1IZ IM
ILLARIONrtV VV
SEARCH FOR CATALYSTS FOR THE OXIDATrON OF SULFUR-DIOXIDE
WITH A DECREASED IGNITION TEMPERATURE
VANADIEVYE KATALIZATORY OLYA KONTAKTN. PROI ZV. SERNOI .KI SLOT Y
NAUCHN-ISSLEO.INST. UDOHR I I NSEKTOFUNG. . SB. ST ATE I 1963
36-42 CA-60-3523
GERHER55POO GERHARD ER JOHNSTONS HF
PHOTOCHEMICAL OXIDATION OF SULFUR-DIOXIDE IN AIR
IND.ENG.CHEM.47,972-6(I 15551
GERNDV35TEO GERNET 0V KHITUM
THE EFFECT OF METAL OXIDE ADMIXTURES ON THE ACTIVITY OF THF
TIN CHROMIUM CATALYST
J.APPLIED CHEM.(USSRIB,598-604(1935)CA-30-360l-4
GEYSK 650QW GF.YS
FUERST H
PURIFICATION OF HASTF LIQUIDS AND GASES
FR.1,406,577 (CL.B 01D.C C2 OJULY 23,1965 GEP . APPL. APR. 6
GIGNJ 67FBM GIGNIEP JP
FIXED-BED CATALYTIC REACTORS i. MAIN PROBLEMS
CHIM. INC., GENIE CHIM. 98( 10) . 1 694-9( 1 967 I FP CA-68-88452 M
GILREE64SLT GILBERT EE
STABILIZING LIQUID SULFUR-TR IDXIHE WITH PHOSPHORUS
CONTAINING COMPOUNDS
FR. 1,349,057 (CL. C "MR I .JAN. 1,1964 U. S. APPL . MAR.8 , 1 96?
CA-61-IPI-7984C
GIOLF 67EPP GIOLA F
EFFECTS OF POISONS ON POROUS CATALYST ACTIVITY
CL-SC1- F"..MAT.NAT.42f4,,515
GIOLF 67EPP GIOLA F
EFFECT OF POISONS ON POROUS CATALYST ACTIVITY
GISTAM37TCO GISTLING AM
THE CONTACT OXIDATION OF SULFUR-niPXIDF. TO SULFUR-TP IPXI RE
UNDER PRESSURE
J.CHEM.INn.(USSR)l4,5i;»-16(1937) CA-31-551R-7
GLADVI63TVO GLADUSKO VI
THE VELOCITY OF ACID FORMATION IN THE °RESFNCE PF SALTS IN
N I TROS E
1ZV. VYSSHIKH UCHEBN.^ZAVEDENI I, KHIM I KH I M. TEKHNDL .fel 6)
GLASV 66COT GLASER V RHUSAR I
CALCULATION OF THE RATE OF A HALF ORDER REACTION PROCEEDING
IN PORES OF A CATALYST
COLLECTION CZECH. CHEM. COMMUN.31 1 5 1 . 2137-43 1 1 966) ENG
GOHLRS66M.S* MJ^IpElT-OMETRV o^lSlEs PROnUCING SULFUR-TRIOXIDE
ANAL. CHIM. ACTA.36141,530-21196MFNG CA-66-34334 0
GOLOT 64SST GOLOSCHMIDT T
STABILIZING SULFUR-TRIOXIOE
GER. 1.175,656(CL. C 01BI,AUG.13.1964,APPL.APR.25,1963
CA-61-IPI-14233E
GHLFF 62GCM GOLF F LORENZ F
GAS-CHROMATOGRAPHIC METHODS FOR TESTING CATALYSTS
ABHANDL. DENT. AKAD. MISS. BERLIN, KL. CHEM.,GEOL. RIOL.1962
(11,507-11, CA-59-4581 E
GOLOGI63EOT
GOLOOETS GI
ENTROPY ~
'Y OF THE ACTIVE COMPLEX IN THE OXIDATION OF
SULFUROUS-ANHYDRIOE OVER PT CATALYST
MNETIKA I KATALIZ M 5» , T76-9( 1963» CA-60-Z3f>7 0
GOLONA66ARO GOLOVKO NA BRODOV ICH KI ZAV'YALOVA ND
UU ALKALINE REGENERATION OF VANAOIUM FROM SPENT CATALYST FROM
SULFURIC-ACIO PRODUCTION
KHIM.PROM. UKR.IRUSS EO. 1 1 966( 5 1 , 49-5 1 ( RUSS 1C A-66-2 1 207A
GOROYB66EOS
GO R OK HO V AT S I
REACT,N(. MOLECULES ON RECULAR,T,ES
OF THEIR CATALYTIC TRANSFORMATION
KATAL.KATAL., AKAD.NAUK UKR. SSR .RESPUB. MEZHVEDO*. SB. NO. 2
5-251 1966IRUSS CA-66-59215
GRADLI62POC Gg ADUSOVA^ f C4TftLYSTS ,„ ft FLU,DIZEO LAYER FOR 0xiDATION
VEsfN^TEKHNTD{°EKON, INFORM NAUCHN.- I SSLED. INST. TEKHN.-FKON
ISSLED.GOS.KQM.SOV.MIN. SSSR PO KHIM. 1 P62 I 9) , 1 f--l 7
CA-60-11412 H
GRADLI63COO GRAOUSOVA LI SULFUR-OIOXI DE GAS IN A FLUIDIZED BED
VESTN.TEKHN.I EKON. INFORM. NAUCHN. -I SSLED. I NST. TFKHN.-EKON.
ISSLED.GOS.KO^.SOV. MIN.SSSR PO KHIM 1963(11,23 CA-6C-1 5468C
GRAS 36SG
GRECG 56COO
GPIGAF6BPCC
GRASSELLI CHEMICAL CD.
BRIT.*448^125 JUNE 2,1936 CA-31- ( PI -72 10-8
OXIDATION OF SULFUR-DI OX| DE TO SULFUR-TRIOXI OE
BRIT. 749,645, MAY. 30, 1956 C A- 5C- ( P I - 1 0059-B
GR1GOROV AF GRISHINA NM IPFFE II
PREPARING CORUNDUM CARRIERS FOP. CATALYSTS
BRIT. 1,100,516 (f.L. B 01 J 1 , JAN. 24 , |9f-8.API'L . NOV. 4 ,
CA-68-CM-79977 R
133
13k
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33
GRILW 66RSC MgVAL OF SULFUR COMPOUNDS FROM FLUE-GASES
NETH. APPL. 6,601,639 (CL.B 0101 AUG. 11 ,1966 CA-66-P-12305 0
GRODMK33COO GPODZOVSKI1 HK
CATALYTIC OXIDATION OF SULFUR-DIOXIDE PRESENT IN FLUE-GASES
BY IONIZED SOLUTIONS OF HEAVY METALS
IZVESTIYA TEPLOTEKH. INST.N0.4,22-36(1933 ICA-27-5899-4
GRODMK35HOT GRODZOVSKII HK
MECHANISM OF THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE IN A
SOLUTION OF MANGANESE SALTS
J.PUTS.CHEH.I USSR 16,478-951 1935) CA-30-2CI90-B
GROS'A 65SOA GROSSMAN A
SULFUR-OXIDES AND OTHER SULFUR COMPOUNDS A BIBLIOGRAPHY WITH
ABSTRACTS
U.S.GOVT. PRINTING OFFICE 1965 CA-63-9438 F
GRUNE 66POI
GUPTAD67TCB
GUPTAD67TCS
GPUNDKE E ROEOER U
PORE DISTRIBUTION IN POROUS CATALYSTS
CHEM.TECHI BERLIN I 181 121, 727-30(19661 GER
CA-66-59230 R
GUPTA AD
THERMAL-CONDUCTIVITY OF BINARY MIXTURES OF SULFUR-DIOXIDE
AND INERT GASES
INST. J.HEAT MASS TRANSFER 10)7),921-9119671ENG CA-67-57815G
GUPTA AD
THE '
HERMAL CONDUCTIVITY OF SULFUR-DIOXIDE AND DIETHYL-ETHER
AT DIFFERENT TEMPERATURES
INDIAN J. PHYS 41(6),419-2511967IENG CA-68-70SO 0
GUYAGL66SPF GUYAT GL
SNPA'S PROCESS FOR H2S04 PRODUCTION DEVELOPED WITH EVE ON
AIR POLLUTION
OIL.GAS J. 64(47»,198-200(1966)ENG CA-66-57396 A
HALLCC67CTP
HAMOJP66CPA
HANPG 62SSO
HAMPG 64CSA
HALL CC
CATALYSIS THEORY AND PRACTICE
CHEM. BRIT. 3« 71 , 305-6( 1967IENG
CA-67-12037B J
HAMOUX JP
COMPUTER PROGRAM FOR AN ADIABATIC CATALYTIC REACTOR
CHIN. IND.,GENIE.CHIM. 95C61,1389-92119661FR. CA-6S-16521 H
HAMPRECHT G MEISIEL H
SEPARATION OF SULFUR-OXIDES FROM WASTES GASES
BRIT. 896.457,MAY 16,1962 CA-57-CPI-5588 0
JOERGFR K
FEILER P
HAMPRECHT G JOE....
CATALYST FOR SULFURIC-AC ID PREPARATION
GER. 1,171,404 (CL. C 01BI.JUNE 4,1964,APPL. DEC.14,1962
CA-61-(PI-3961 C
HAPPG 64SAR
HAHPNH65EEA
HAMPRECHT G
SULFllRIC-ACrO
FR. 1,369,945 (CL.
JOF.RGE" K FEILER P
C Oil)) ,AUG. 14.1964 CA-63-(PI-392S E
HAMPSON NH
ECONOMIC ELIMINATION OF AIR POLLUTION THROUGH RECOVERY
PRODUCTS IN POLYESTER GAS SCRUBBERS
ALLG. PAPIER-RUNDSCHAU NO. 21, 1392, 1 394 ,1396( 1965 )GER.
CA-66-M83A S
HAPPPJ64SCP HAPP PJ MUNRO JG
SOME CORROSION PROBLEMS IN A HEAVY CHEMICAL AND NONFERROUS
SMELTING WORKS
AUSTRALASIAN CORROSION ENG. 8( 7| , 9-15( 1964 IENG CA-66-4503 E
HA9AH 57HOC
HARAH 5BCRR
HARA H
MEASUREMENT OF CATALYTIC OXIDATION RATE OF SULFUR-OIOXIDE
KOGYtl KAGAKU ZASSHI GO, 1255-7(19571 CA-53-13755 A
HARA H
CONTACT REACTION RATE OF S02 OXIDATION
THE RATE BY A DIFFERENTIAL METHOD
RYUSAN 11,136-91(19581 CA-54-3032 I ,3033 A.B
DETERMINATION OF
HARAH 59CRM HARA H ADACHI A
CONTACT REACTION RATE OF S02
OXIDATION
THE RATE OF FOUR DIFFERENT FEED GASES
RYUSAN 12,155-60(1959) CA-54-25620 B
KURATA N
MEASUREMENT OF
HARAH 59CR4 HARA H A04CHI A KURATA N
CONTACT REACTION RATE OF S02 OXIDATION APPLICATION OF THE
RATE EXPRESSION TO NEW OBSERVATIONS AND ILLUSTRATION FOR
THE CONVERTER DESIGN
RYUSAN 12,155-60(1959) CA-54-25620 B
1-4PAH 59RRO HARA H AOACHI A KURATA N
REACTION RATES OF CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH
VANAOIUM-PENTOXIOE CATALYSTS
KOGYO KAGAKU ZASSHI 62,669-72(1959) CA-57-7965 C
HARAH frOTCO HAPA H AOACHI A KURATA N
THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH VANADIUM
CATALYST
KOGYO KAGAKU ZASSHI 63,56-9(19601 CA-56-2025 H
HARAY 630RR HARANO V
DIFFUSION AND REACTION RATE
KAGAKU TO KOGYO(TOKYO) 16,306-16(1963) CA-61-6439 E
HARLEV56CdS HARLOW EV
CONDITIONING OF STACK GASES FOR ELECTROSTATIC PRECI PITATORS
U.S.2,746,563,MAY 22.1956 CA-5P-(P)-12499 F
6C.DTM HARMELIN
DETERMINATION OF TRACES AND THE MICROANAL YSIS HF GASES
AND VAPORS
CHIM. ANAL. (PAR ISM 4) , I97-2P7(1966IFR. CA-65-4636- .O
135
136
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HART 67FOC
HARTJS67EOI
HAUEAP650MG
HARTER MO
FIND OPTIMUM CATALYST REGENERATION CYCLE
HYDROCARBON PROCESS. 461 51 ,181-61 19671 ENG CA-67-34537 V
HARTMAN JS
EFFECTS OF
ROBERTS GW SATTERFIELO CN
INITIAL CONOITIONS ON THE STEADY STATE ACTIVITY
OF CATALYST PARTICLES
IND.ENG.CHEM., FUNDAM. 6(11,80-3(1967)ENfi CA-66-49595 I
HAUEL AP
OPEN MESH GLASS-FARRIC SUPPORTED CATALYST
U.S.3,189,563(CL.252-4iSP) tJU " " "~~
DEC.1,1960 CA-63-(P)-4993 D
.252-4ISPI.JUNE 15,1965,APPL.MAY 14.195R AND
HAUFK 65RFH HAUFFE K
ROLES OF ELECTRONS HOLES AND LATTICE DEFFECTS IN
HAY JG2PCCA
HAYNFG67NSA
HETEROGENEOUS CATALYSTS
ANALES REAL SRC. ESPAN. FIS. OUIM. (MADR ID) , SER. R 61(2)
277-39ZI 1965IENG CA-63-10737C
HAY JG
COLLOIDAL CLAY AS CATALYST IN OXIDATION ANO HYOROGENATI ON
CHEM.AGE 2,194(1920) CA-14-1070-3
WILLIAMS K
EVANS TE
HAYDES FG
BARKER W
NICKEL SILICON ALLOYS
GEP. 1,243,397-101531 N
HOFMH 64SPF HOFMAN H
STANDARD PROGRAMS FOR THE OPTIMIZATION OF PROBLEMS IN
CHEMICAL TECHNOLOGY
OFCHEMA MONOGRAPH 53(912-929IGER. CA-64-4235 0
HOHMH 67LMD HOHMANN H HUCKAUF H
LIMESTONE MILL DRYING PLANTS FOR THE REMOVAL OF SO?
FROM HASTE AND FLUE-GASES
CHEM.TECH.I BERLIN) 19( 9) , 533-6, ( 1 967)GER. CA-A8-15831 Z
HOHMH 6 77-( P)-76I24 X
137
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10/27/69
PAGE 37
HOLMHN29PSG HOLMES HN R4MSAY J FLDER AL
PLATINIZED SILICA-GELS AS CATALYSTS FOR THE OXID
OF SULFUR DIOXIDE
IND.ENG.CHEM. 21,830-311929) CA-23-527B-10
ATION
HPLHHN30VCA HOLMES HN
ELDER AL
VANADIUM COMPOUNDS AS CATALYSTS FOR THE OXIDATION OF
SULFUR-DIOXIDE
IND.CHEM.ENG 22,471-31 193C ) CA-74-3089
HOL1WC65CRH HOLMES WC
CHFMICAL REACTIONS BY ELECTRICAL DISCHARGE
RRIT. 1,009,3311CL.C 01B)iNOV.1Of1965,A PPL.NOV. 12,1960
CA-64-6142-H
HOLZH 65RON HOLZMANN H
RECOVERY OF NOBLE METALS EVAPORATED FROM AMMONIA-OXIDATION
C AT AL YSTS
GER. 1,207,089 (CL . C 22BI.DEC. 1 6,1965, APPL. OCT.3,1964
CA-64-(P 1-9284 B
HGMMAC61SAO HOMME AC DTHMER DF
SULFURIC-ACIO OPTIMIZED CONDITION IN CONTACT MANUFACTURE
INO.ENG.CHEM.53,979-841 19611 CA-56-15147 G
HOPAJ 67HAM HORAK J MAMULA P
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS II. THE
EFFECT OF CATALYST CONDUCTIVITY ON THE APPARENT
CONDUCTIVITY OF THE CATALYST BED AND THE HEAT TRANSFER
COEFFICIENT FROM THE BED TO REACTOR BATH
CHEM.PPUM. 17(41 188-9K1967KZECHI CA-67-55555 Y
HOFSGF46AC HORSLEY GF
ACTIVATING CATALYSTS
U.S. ?, 408, 396,OCT. 1, 1946 CA-41-(P)-577A
HORSG«=47AOC HORSLEY GF
ACTIVATION OF CATALYSTS
BRIT. 589,795,JUNE 30,1947 CA-41-(P)-7066 D
HUEGG 67PCG HUEGL I G
RFACTOR FOR CATALYTIC GAS REACTIONS
SWISS 430,663 (CL.B 01JI.AUG. 15,1967,APPL. MAY 25,1966
CA-68-(0)-60844 S
HUPTDM40CCS HURT DM
CATALYTIC CONVERTER SUITABLE FOR OXIDIZING S02 TO S03
US. 2,246,684,JUNE 24, CA-35-(PI-6074-2
HUPTDM43POR HURT 0"
PRINCIPLES OF REACTOP DESIGN GAS-SOLID INTERFACE REACTIONS
INO. ENG. CHEM. 35.522-8(1943) CA-37-40"l-4
HUTCJ 66ISC HUTCHINGS J CARBERRY JJ
THE INFLUENCE OF SURFACE COVERAGE ON CATALYTIC EFFECTIVENESS
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A.I.CH.E. J.12(ll,20-3(1966IENG CA-64-11913 E
HUTTJC65PAA HUTTER JC
POROUS AC
BELON P
.TIVATED ALUMINA OF HIGH MECHANICAL STRENGTH
FR. 1 386,364 (CL.C 01FI.JAN. 22,1965,APPL.DEC. 2,1963
CA-62-(P)-13902G
HORVT fr*RSO HORVATH T
RECOVERY OF THE S02
CONTENT OF FLUE-GAS WITH THE
FERDINAND Z
U 1 TH THF
SIMULTANEgys7_PROOUCf ION "bF~MAGNESITF~"JSINTER
HUNG. 152,841 (CL. C 0 IB, F I ,MA Y 22~, 1966 APPLl' MAY 25,1965
CA-65-1PI-10184 F
HOUGOA43SCA HOUGEN OA WATSON KM
SOLID CATALYSTS AND REACTION RATES GENERAL PRINCIPLES
INO. ENG. CHEM. 35 529-41(19431 CA-37-4?o«-!i
HflUS 67FGC HOUSEMAN t THOMPSON LTD.
FLUE-GAS CORROSION REDUCTION
BRIT. 1,088,504 (CL. F 23J),OCT. 25,1 '167 , APPl . MAY 8,1964
CA-68-(PI-51860 S
IGREV 67ACS IGREJA V
AN AUTOMATIC CONTROL SYSTEM FOR THE DRYING AND ABSORPTION
CYCLE IN SULFURIC-ACID.PRODUCTION
TECNICA (LISBON) 42(364),167-B2I1967)PORT. CA-67-660B4 V
ILCHNI67TIO IL'CHENKO NI YUZA VA ROITER VA
THE INFLUENCE OF SMALL QUANTITIES OF ADDED PLATINUM ON THE
CATALYTIC ACTIVITY OF VANAOIUM-PENTOXIDE REGARDING THE
OXIDATION OF HYDROGEN
DOKL. AKAD. NAUK SSSR 172(1),133-6119671RUSS C4-66-108681 Z
ILLAVV55PCO ILLARINOV VV
PHASE CONDITION OF ACTIVE COMPONENT IN VANADIUM CATALYSTS
OF SULFUR-DIOXIDE OXIDATION
S BORN IK 1955,393-5 REFER AT .ZHUR . ,KHI M. 1 95ft CA-52-17637 B
INGE 25CCA INGENUIN HECHENBLEIKER
CATALYTIC CONVERTER APPARATUS SUITABLE FOR OXIDIZING
SULFUR-DIOXIDE
US.I,782,824,NOV. 25, CA-25-(P)-387-2
INST 66SEO INSTYTUT CHEMII OGOLNEJ
SHAPED ELEMENTS OF CATALYSTS FOR CATALYTIC REACTIONS IN
GASEOUS PHASE
POL. 51.920ICL.B 01J )OCT.8. 1966 CA-68-( PI-A3101 H
INST 67BCU INSTYTUT CHEMII OGOLNEJ
BLOCK CATALYST USED IN THE CATALYTIC REACTIONS IN THE GAS
PHASE
FP. 1,466,537 (CL. B OU) JAN. 2P, 1"67. CA-67-1») -68025 A
IRVIHB51DOF IRVIN HB OLSON RW SMITH JM
DESIGN OF FIXED-RED CATALYTIC REACTORS
CHEM.ENG.PROGRESS 47,2S7-94(19MI CA-45-6437 C
139
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38
PAGE
39
ISENH026CAS
ISENBERG.HO
ATALYT1C APPARATUS SUITABLE FOR CONVERSION OF
SULFUR-DIOXIDE TO SULFUR-TRIRXIDF
US. 357, 308 HAY ID CA-26-( P 1-3885-6
ISHIT 65KOT ISHII T
KINETICS OF THE OXIDATION OF SULFUP-OI OXI OE WITH A POISONED
COMMERCIAL VANADIUM CATALYST
B.CGAKU KOGAKU 29(101 ,779-84( 1965) JAPAN CA-65-3061 C
ISHIT fcfiACO ISHII T
A CRITIQUE ON THE ACTIVITY TEST OF COMMERCIAL CATALYSTS
SHOKUBAI (TOKYO) 8( 2 1 , 143-91 1966IJAPAN CA-66-69290Z
ITKIDY52KOA
IVAND 64SAH
ITK INA DY MALIN KM
KINETICS OF ACID FORMATION
J.APPL.CHEM.USSR 25,108-95(1952) CA-49-4243
PASTUKHOVA MG
I
IVANOV 0 KOSTADINOV N
SIMULTANEOUS ABSORPTION OF HYOROGEN-SULFIDE AND
S3? BY AMMONIUM-SULFITF-BISULFITF. SOLUTIONS UNDER
SEMI-COMMF.RCIAL CONDITIONS
GOO IS HN IK KHIM.-TECKHNOL. INST. 11 M) ,53-64 (I 964 I (PUB.1965)
(BULG.) CA-66-4443P
IVANRS62POV IVANOVA RS MUKHLENOV IP
POISONING OF VANADIUM CATALYST IN A FLUI Dl 7.ED-BEO WITH
ARSENIC-TRIOXIOE
ZH.PRIKL.KHIM.3AI4), 737-421 19621 CA-5°-334fl B
JACKPJ59VTC JACKSON PJ FIELDER RS PAASK F
THE VARIATION WITH TEMPERATURE OF THE CATALYTIC ACTIVITY
OF «N OXIDIZED STAINLESS STEEL SURFACE IN THE OXIDATION
CF SULFUR-DIOXIDE
FUEL 33,257-8(1959) CA-53-1115C H
JACOA 66RSO JACOS A WESTBURY RA WINKLE* CA
REACTION OF SUlFUR-DIOXinE WITH ACTIVE NITRDGEN
J. PHYS. CHEM. 70( 12),4066-8( 1966)ENG CA-66-34431 U
JAEGA022COO JAEGFR AQ BERTSCH JA
CATALYTIC. OXIDATION OF SULFUR-DIOXIDE
U.S. 1,657,7S3,JAN. 31. CA-2?-(PI-l018-5
JAEGA023COO JAEGER AO BERTSCH JA
CATALYTIC OXIDATION OF SULFUR-DIOXIDE
US. 1,696,5*6,DEC. 25 CA-23-(P1-940-2
JAEGAOZ7SA JAEGER AO
SULFURIC-ACIO
SKIT. 29*,975,AUG.3,19?7 CA-?3-(P)-199S-2
JAEGA028CA JAEGER AO
CATALYTIC APPARATUS
BRIT. 306,44?,FEB.20,19?R
JAEGAHZHCAF
JAFGA!)30COO
JAFFJ 610C
JAFFS 66PC1N
JANIW 67MFP
JAEGER AH
CATALYTIC APPARATUS FOR GAS REACTIONS
BRIT. 306,r.l9,FEB.23, 192H CA-2 3-I P)-4851
CATALYTIC DXIOATION OF SULFUR-DIOXIDE TO TRIOXIDE
US. 1,885,833,NOV.1 CA-27-(PI-11 09-9
JAFFE J
OXIDATION CATALYSTS
U.S. 3,202,618(CL.252-469),AUG.2*.196?,APPL.JUNE 5,1961
CA-63-(P)-172C6 D
JAFFE S KLEIN FS
PHOTOLYSIS OF N02 IN THF PRESENCE OF S02 AT 3660-A
TRANS.FARADAY SOC. 6218),2150-7119661 ENG
KRAWIFC I
GAJEWSKI A
JANICEK W
MECHAN?SMZFOR RECOVERY OF PLATINUM LOSSES DURING AMMONIA
CATALYTIC OXIDATION
PREM.CHEM. 46(91,547-5011967IPOL. CA-68-23198 P
JASPHP6SMAS JASPER HP
KREDZ RJ
METHOD AND APPARATUS FOR SUBDIVIDING PARTICULATE SOLIDS
U.S. 3,219.281 (CL. 241-5 I.NOV.23,1965,APPL.JULY 8,1963
CA-64-IPI-4637 C
JAVOJ 66FRP JAVORSKY J ANOERSSON AL
FLUIOIZED BED PROCESSES
U.S. 3,261,661 (CL.23-1) JULY 19,1966 CA-65-58G
CATALYSTS SUITABLE FOR USH IN OXIHATII1N OF
SULFilR-OIOXIOF.
1.1. 5.2,0*6, 166. JUNE 1.", r.ft-1C-(P)-574:->-4
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PACE 41
JIPUP 5TSSC JIPU P Rsm.L J
SUPFACF STRUCTURE HF KIFSELGUHR CARRIFWS AND CATALYSTS FOR
THF OXIDATION OF SULFUR-ninxIDE
CHE". PRUMYSL 7,652-4(19571 CA-52-14994 A
JIRUP 59DEC JIRU P
JIRll I
DATA FOR COMPUTATION OF VELOCITY CONSTANTS OF THE CATALYTIC
OXIDATION OF SULFUR-9IOXIOE (IN VANADIUM CATALYSTS
CHEM. PRUMYSL 9,570-5(1959) CA-54-3877 C
TtlMKflVA D
JARA V
JI°'JP 60103 JIRU P
WANKOVA J
INFLUENCE OF ALKALI SULFATED ON THF ACTIVITY OF
V2Q5 IN THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
7.4.NORG.U.ALLGEM.CHEM.303, 121-6( 1960) CA-54-11672 E
JIRUP 61EAV JIRU P JARA V
EFFECT OF ALKALI METAL SULFATES ON THE ACTIVITY OF
V205 FOR THE CATALYTIC OXIDATION OF SULFUR-DIOXIDE
ACTES INTERN. CONG. CATALYSE,2 E.PARIS,1960 2,2113-18
DISCUSSION 2119(PUB.1961) CA-55-23H09 H
JIRUP 63E?T J IRU P
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVITY OF
VANADIUM-PENTOXIDE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE
VANADIEVYE KATLIZATORY DLYA KONTAKN.PROIZV.SERNOI KISLOTY
NAUCHN.-ISSLED.INST.UDOBR. I INSEKTOFUNG.,SB.STATE I 1963
21-35 CA-60-2370 G
JIRJO 63VPC JIRU P
EFFECT OF THE ALKALI METAL SULFATES ON THE ACTIVITY PF
V4NABIUM-PENTOXIDE IN THE CATALYTIC OXIDATION OF
SULFUR-OXIDE
VASADIEVYE KATALIZATflWY DLYA KDMTAKTN. PROIZV. SERNO.
•USLDTY.NAUCHN.-ISSLEO. INST. UDOHR. I INSEKTOFUNG. .SB
STATEI 1963,21-35 CA-60-2570 C,
STEWAPT WE
E STRUCTURE AND GASEOUS DIFFUSION IN SOLID CATALYSTS
J.CATALYSIS 4(2) 248-5?< I9651FNG CA-62-12486H
JQH.MMF65PSG J"H\SON HF STFWAOT WE
°C"E STRUCTURE AND GASFHUS DIFFUSI'lN IN SPLID CATALYSTS
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ULTRASHNICALLY tCTIVATEO CATALYSTS FOR CHEMICAL REACTION
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JUDAW 67EOL JUDA W
EFFECT OF LOW-COST ELECTROLYTIC HYDROGEN ON THE GENERATION
OF BASIC CHEMICALS
CHEM.ENG.PROGR.,SYMP.SER.63(711,59-62(1967)ENG CA-67-2R713 S
JUENH CEA JUENTGEN H PETERS W
CHEMICAL ENGINEERING ASPECTS FOR SULFUR-DIOXIDE REMOVAL
FROM WASTE-GASES
STAUB 25( 10l,425-9( 1965IGER. CA-64-12226 0
JUENH 65CEA JUEMTGER H PETERS H
CHEMICAL ENGINEERING ASPECTS FOR SULFUR-DIOXIDE REMOVAL FROM
WASTE-GASES
STAUB 25 ( 101,425-91 196SIGER.
JUENH 66DSS
KADLB 6600S
JUENTGEN H
DRY SEPARATION OF SULFUR-DIOXIDE FROM WASTE GASES
CHEM.INGR.-TECH. 38(71,734-611966IGER. CA-65-R-13265D
KADLEC B
VOSOLSOBE J
OXIDATION OF
CHEM. PRUMYSL
MICHALEK J
SIMECEK A
S02 IN AN ADIABATIC CONVERTER
16( 51 , 260-2 1 1 966) CZECH CA-65-3364
KALUAE65ARS KALUSHIN_AE
KALUF 65CRC
ABSORBENTS FOR THE RECOVERY OF SULFUR-DIOXIDE
AZERB. NEFT,
44(21 ,35-7( 1965)RUSS CA-64-5785H
KALUZA F MICHALIK J
CORROSION RESISTANCE OF CR-NI WELDS IN ATMOSPHERES
CONTAINING SULFUR COMPOUNDS
PRZEGLAD SPAWALNICTWA 17( 8 ) , 185-9( 1 9651 POL CA-64-17193 E
KAMIY 67DCP KAMIMURA V
THE DOUBLE CONTACT PROCESS Of SULFURIC-AC10 MANUFACTURE
RYUSAN 201B),167-77C19A7)JAPAN 67-51398X
KANEY 65MOS KANEKQ Y OOANAKA H
MECHANISM OF THE OXIDATION OF SULFUR-DIOXIDE
DETERMINATION OF THE STOICHIOMETRIC NUMBER BY MEANS OF S35
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CA-64-5801 G
KAPUAF36CEU KAPUSTINSK
PUSTINSKII AF
EMICAL EQUILIBRIA IN
PHYSIOCHEMICAL FORCE
TRAN. ALL-UNION SCI. RESEARCH
5-12(19361 CA-31-486S
INORGANIC SYSTEMS
S IN A CRYSTAL.LATTICE
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GL AS. HEM. DRUS..BF.OGR AD. 301 4-6 ). 207-16119651 SERBIAN
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KARMM034TIO K ARMA.NDAR> Y AN MO BRODOVICH Kl
THE INFLUENCE OF CARRIERS ON THE CATALYTIC PROPERTIES OF
VANADIUM-PENTOXIOE
J.APPLIED CHEM.(USSRI 7.725-811934> CA-29-2699-5
KARTMB66MDO KARTSVNEL MB TRIKtLO AI
MATHEMATICAL DESCRIPTION OF THE OXIDATION OF SULFUR-DIOXIDE
INTO SULFUR-TRIOXIDE DURING WET CATALYSIS
KHIM.TE*HNOL.,RESPUB.MEZHVEDOM.NAUCHN.-TF.KH.S8. NO.6 89-97
U966IRUSS CA-68-7048 V
KASALA64IEF KASATKINA LA SHUSTOV VI
ISOTOPE EXCHANGE FOR THE OXYGEN OF VANADIUM-PENTOXIDE WITH
SULFUR-DIOXIDE AND TR10XIDE
KINETIKA I KATALIZ 5( 51 > 945-81 1964) RUSS CA-62-2284 C
KASAS 66EFC
KASAOKA S
EFFECTIVENESS
SAKATA Y
FACTORS OF CATALYST PARTICLES WITH SHAPE
DIFFERENCES
KAGAKU KOGAKU 30171,650-611966IJAPAN CA-66-22652 0
KASAS 66EFO KASAOKA S SAKATA V
EFFECTIVENESS FACTORS OF CATALYST PARTICLES WITH SHAPE
DIFFERENCES
KAGAKU KOGAKU 30171,650-611966(JAPAN CA-66-22652 D
KASAS 67C1CE
KASAOKA
OVERAL
SAKATA Y
CATALYTIC EFFECTIVENESS FACTORS AND THEIR SHAPE
CORRELATIONS WITH MASS TRANSFER AND REACTION ON THE
EXTERNAL SURFACE
KAGAKU KOGAKU 3l(21,164-71(19671 JAPAN CA-67-85345 X
KASHLI35IOT
KASHTANOy LI
piM7unu up
INFLUENCE OF TEMPERATURE ON THE OXIDATION OF SULFUR-DIOXIDE
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POISONS
IZVESTIYA TEPLOTEKH.INST.INST.1935.N0.8.43-7 CA-30-3596-6
KASHLI35TKO KASHTANOV LI RUIZHOV VP
THE KINETICS OF OXIDATION OF GASEOUS SULFUR-DIOXIDE IN
AQUEOUS SOLUTIONS AND POISONING OF MANGANIC-SULFATE BY
PHENOL
IZVESTIYA TEPLOTEKH. INST. 1935,NO.7,37-40.CA-30-3596-2
KASHLI36FOI KASHTANOV LI RUIZHOV VP
FORMATION OF INTERMEDIATE COMPOUNDS IN THE OXIDATION OF
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J.GEN.CHEM. I USSR I 6, 549-541 19361 CA-3O-5732-3
KASHLI36TEO KASHTANOV LI
RUIZ VP
THE EFFECT OF HIGH CONCENTRATIONS OF SULFUR 1C-AC ID ON THE
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J.CHEM.IND.IUSSR.il3,1275-BI1"361 CA-31-1963-3
2C5
KASHLI3BASB KASHTANOV LI
A STUDY BY THE OPTICAL METHOD
OLESHCHUK
8N
F THE BEHAVIOR OF THE
MANGANESE SALT CATALYST IN STRONGLY ACID SOLUTIONS IN
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J.GEN.CHEM.(USSR I 8,341-5(19381 CA-32-5285-9
KASHLI3800S KASHTANOV LI
OXIDATION OF S
RYZHOV VP
ULFUR-OIOXIDE BY OZONE IN THE PRESENCE OF
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J. GEN. CHEM.IUSSRJ8, 746-501 19381 CA- 33-818-3
KASHLIS4MOI KASHTANOV LI
LUK'YANOV AB
MECHANISM OF INHIBITING ACTION
TRUDY HOSKOV. INZH.-EKON. INST..KHIM.I KHIM PROIZVODSTVO
1954 NO.1.135-8 CA-50-11089 H
KATES 66RSD KATELL S
REMOVING SULFUR-DIOXIDE FROM FLUE-GASES
CHEM. ENG. PROGR. 62 I 101.67-7311966IENG CA-66-5553H
KATOA 62TCO KATO A
THERMODYNAMIC CONSIDERATION OF CATALYTIC OXIDATION
MEM. FAC. ENG. KYUSHN.UNIV. 21.133-52(19621 CA-58-965 G
KAUTO 66RCE KAUTSKY 0
REACTOR FOR CATALYTIC EXOTHERMIC REACTIONS AT ELEVATED
TEMPERATURE
CZECH. 120,646 (CL B 0U>,NOV.15,1966,APPL.MARCH 18.1964
CA-68-IP 1-31446 H
KAWAT 54TPP KAUAGUCHI T
MECHANISM OF THE CATALYTIC OXIDATION OF S02 CONSIDERED
FROM THE THEORY OF SEMICONDUCTOR CORRECTION OF THE
MECHANISM OF CALDERBANK
J.CHEM.SOC.JAPAN.PURE CHEM.SECT. 75,835-8(19541 CA-49-5943 F
KAWAT S500S KAWAGUCHI T
OXIDATION OF SULFUR-DIOXIDE BY N-TYPE SEMICONDUCTOR CATALYST
J.CHEM.SOC.JAPAN PURE CHEM. SECT. 76. 1112-1 511955 I
CA-50-8302 8
KA2AE164SCI KAZAKOV El
MELENT'EV PN
CHERNVKH VI
SHAPING OF CATALYSTS INTO SPHERICAL GRAINS
NAVCHN. OSNOVY PODBORA I PROIZV. KATALIZATOROV.AKAO.NAUK
SSSR.SIBIRSK.OTD. 1964.480-5(RUSSI CA-63-6363 H
KAZAYZ66UTS KAZAVCH INSK11 YZ
USE_pF_THERMODVNAMIC
JOASHEV VI NEDOSTUP VI
.._ SIMILARITY FOR THE DETERMINATION OF
BOYLE-CURVES OF SUBSTANCES STUDIED IN A LIMITED
TEMPERATURE INTERVAL
TEPLOFIZ. VYSOKIKH TEMPERATUR.AKAD.NAUK SSSR 4(41.513-17
(1966IRUSS. CA-65-17724 F
KA2IC 67FBO KAZIZ C
FIXED-BED CATALYTIC REACTORS II. ONE DIMENSION STATIC MODELS
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CHIM.IND.,GENIE CHIM. 9811Ql.1709-Q(19671FR- CA-68-B845Z N
206
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MUKHLENOV IP
SLIN'KO MG
KFRNVS6600S KERNERMAN VS
FILATOV YV
OXIDATION OF S02 IN A FLUIDIZCO CATALYST RF.D
KHIM.PROM. 42( 6),443-5( 1966IRUSS CA-65-18186 A
KESTU 65SCT KESTERNICH H
SIGNIFICANCE OF CORROSION TESTING PROCESS WITH SPECIAL
CONSIDERATION OF THE S02 TEST ACCORDING TO OIN-V1018
MERST. KERROS. 16,143-20111965IGFR CA-66-31585
KETTH 65TRO KETTNER H
THE REMOVAL OF SULFUR-DIOXIDE FROM FLUE-GASES
BULL. WORLD HEALTH ORGAN.3213»,421-9119651ENG CA-63-12702 A
KHAROM34TIO KHARMANDAR'YAN ON BRODOVICH KI
THE INFLUENCE OF CARRIERS ON THE CATALYTIC PROPERTIES OF
VANADIUM-PENTOXIDE
J.APPL.CHEH.IUSSRI 7,725-8(1934) CA-29-2699-5
KHOKSF65MTS KHOKHLOV SF
KINGRP65COT
IN
ANNFNKOV VA SHUTKIN GA
A SCRUBBER WITH CONE-SHAPED GRID PLATES
MASS TRANSFER . - - . . . ._
KHIM. I NEFT. MASHINOSTR. 1965191 ,25-6(RUSS) CA-64-3675 G
KING RP
CALCULATION OF THE OPTIMAL CONDITIONS FOR CHEMICAL REACTORS
OF THE COMBINED TYPE
CHEM.ENG.SCI 201 61, 537-44( 1965IENG. CA-63-6620 F
KIPPHB19ACR KIPPER HB.
ACCELERATING CATALYTIC REACTIONS RY RAPID MOVEMENT OF THE
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II.S.I, 512, 225.OCT.21 CA-19--(P 1-6360 D I
KEPNVS63CFB KERNERHAN VS MESHCHERYAKOV VO
CALCULATION OF THE FLUIDIZED-BED CATALYTIC PROCESS
SB.DOKL. NA VSES SOVESHCH. PO MODELIROVANIYU I OPTIMIZATSII
KATALITICHESKIKH PROTSESSOV,!ST.NOVOSIBIRSK.USSR 1963
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10/27/69
KIYOR 40ACO
KIYOR 66POS
KIYOR 66ROS
PAGE 45
KIYOURA R
ACTIVE CENTER OF A CATALYST
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PRECIPITATION OF SULFUR-DIOXIDE FROM HOT FLUE GASES
RAISAKU LUFT 26(121,524-5(1966IGER. CA-66-87175 V
KIYOURA R
REMOVAL OF S02 FROM HOT FLUE GASES TO PREVENT AIR POLLUTION
J.AIR POLLUTION CONTROL ASSOC . 16( 9) ,448-9 (19661 ENG
CA-65-20739 C
KLFEEW 51PAO
KLIMR 64SRS KLIMECEK R
KLEESE H
POSSIBLE APPLICATIONS OF RHENIUM METAL AND ITS ALLOYS
METALL 5,155-6(19511 CA-45-6143 A
KANA B
MIKULSKY R
JAR A V
SANITARY REMOVAL OF SULFUR-DIOXIDES FROM INDUSTRIAL GASES
CZECH.Ill,472 (CL.C 02CI.JULY 15,1»64,APPL. DEC.B,1962
CA-62-(P)-4948 C
KLIMR 65DFG KLIMECEK R SKRIVANEK J BETTELHEIM J
DESULFURIZING OF FLUE-GASES
STAUB REINHALTUNG LUFT 26(61,235-8 (1966IGER. CA-65-I4B97E
KLYAGL62TPO KLYANINA GL SHLYGIN AI
THE POSSIBILITY OF ELECTROCHEMICAL OXIDATION OF
SULFUR-DIOXIDE BY ELECTROLYTIC OXYGEN
SOOBSHCH.OEL'NEVOST.FILIALA.SIBIRS.OTD.AKAD.NAUK SSSR NO 15
27-30( 1962IRUSS CA-62- 10061
KNUDCW66EGC
KOBONI55CAF. KOBOZEV NI
KNUDSON CW ROBERTS GW SATTERFIELD CN
EFFECT OF GEOMETRY ON CATALYST EFFECTIVENESS FACTOR
IND. ENG. CHEM..FUNDAMENTS 5( 3 1 , 325-61 1 966 I ENG CA-65-6347 H
CATALYST AND ENZYME THE PROBLEM OF SURFACE ACTIVITY OF
NATURAL SUBSTANCES
UCHENYE ZAPISKI MOSKOV. GOSUOARST.UNI V.I M. M. V LC1NONOSOVA
NO. 174,125-54(19551 CA-51-5S22 F
.. LFBEDEV VP SHEKHOBALOVA VI
UTILIZATION OF DILUTE ADSORPTION CATALYSTS IN THE CHEMICAL
KOBONI57UOD KOB07EN NI
UTILIZATIOi
INDUSTRY
VESTNIK MOSKOV. UNIV..SER. MAT.,MEKH.,ASTRON.,FIZ.I KHI".
12,NO.5,133-44(1957) CA-52-20773
KOBONI60MOC KOBOZEV NI
MECHANISM OF CATALYSIS
HETEROGENEOUS AND ENZYMIC CATALYSIS
KOEGH 65ROU
VALENCE AND ENERGY FORMS OF
.... ._ CATALYSIS
ZHUR.FIZ.KHIM. 34,1443-58(1960) CA-55-7O02 F
KOE
REA _ _ _ _ _ _
GER^IEAStJ74l7646(CL. C~lOGIiOCT.571965,APPL^JULY 25,1962
CA-64-(PI-7412 H
EGLER H OUECK S
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2C7
208
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OXIDATION OF SULFUR-niHX IDE IN A HIGH-VOLTAGE ARC-DISCHARGE
J. PHY S. CHEM. I USSR (4,845-53(1933 I CA-29-1330-7
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OXIDATION OF SULFUR-DIOXIDE IN A HIGH-VOLTAGE ARC-DISCHARGE
J.PHYS.CHEM CUSSR 15, 1*71-2(1934) CA-29-6153
KONDP 68HMT KONOEL IK P HORAK J TESAROVA J
HEAT AND MASS TRANSFER FOR HETEROGENEOUS CATALYSIS
IND.FNG.CHEM. .PROCESS DES. DEVELOP. 7(2) f 250-2 ( 1 968) ENG
CA-68-88494 B
KON10 52DOA KONISHI 0
DESIGN OF A CATALYTIC REACTOR
CHEM. ENG. JAPAN 16.335-7(1952)
CA-46-10698 E
KOPIR 68MSB KOPITA R GLEASON TG
WET SCRUBBING OF BOILER FLUE-GAS
CHEN. ENG. PROGR. 64( 1 1 . 74-8( 1968 )ENG. CA-68-53005 R
KORMNA66PIP KORMSHCHIKOVA NA BRYNZA AP BELOUS VP
PROTECTION OF IRON POWDER BY THE LEAO-AZELATE
Z ASCH, METAL .21 6 1,668- 70(1 9661 RUSS
KORNG 30TOO KORNFELD G
THE OXIDATION OF !
Z.ELECTROCHEM 36. <
HEEGNANN E
JLFUR-DIOXIDE IN ULTRA-VIOLET LIGHT
39-94(1930)
KORNGP56IOC KCRNFICHUK GP ROITER VA STUKANOVSKAYA NA
RZAEV PB ZHIGAILO YV
INFLUENCE OF CATALYSIS CONDITIONS ON CONTENT OF SULFUR IN
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SULFUR-DIOXIDE
..PRDBLEMV KTNETIKI I KATALI/A, AKAD. NAUK S.S. S. R.. INST. FIZ.
KH1M..SOVESHCHANIE.HOSKOU, 1956 9,329-36(PUB. 1957)
CA-53-7743 H
KOTENZ57COO KOTELKOV NZ
CONTACT OXIDATION OF SULFUR-DIOXIDE AND HYDROGEN-SULFIDE ON
COMPLEX SPIRALS OF PLATINIZED NICHROME
ZHUR.PRIKLAD.KHIM. 30.470-4(1957) CA-51-13541 A
KOTENZ57CDS KOTELKOV NZ
CONTACT OXIDATION OF SU
_ .ULFUR-DIOXIOE AND HYDROGEN-SULFIDE
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J.APPL.CHEM.U.S.S.R. 30.499-503(1957) CA-52-16851A
KOTENZ66UOC KOTELKOV NZ
USE OF CERTAIN CATALYSTS AND ADSORBENTS IN INDUSTRIAL
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TP. SARATOV.SEL-KHOZ.INST. 1(12 I,272-611966IRUSS
CA-66-98261 W
KOWAE 65IUF KDWALSKA E
KQWALSKI W
iNFLUENCE'QF THE ULTRASONJC"FIELD.ON THE CATALYTIC ACTIVITY
OF MN02 PREPARED BY ELECTROLYSIS
DCZK-.-..
KOZAZ 66EON KOZAK Z AKERMAN K
EFFECT OF NUCLEAR RADIATION ON THE ACTIVITY OF VANADIUM
CATALYSTS IN THE REACTION OF S02 OXIDATION
PRZENYSL CHEM 45( 41,1B9I1966IPOL CA-65-8056 G
KOZHNV66PAX KOZHEVNIKOVA NV
TRABER DG
SPECTROGRAPHIC AND X-RAY DIFFRACTION STUDY OF IRON-OXIDE
CATALYST FDR SULFUR IC-AC ID MANUFACTURE
ZH.PRIKL.KHIM. 39(6),1272-5(19661RUSS CA-65-9786 0
KRALH 65DNM KRAL H
DISTRIBUTION OF NOBLE-METALS ON CARRIER CATALYSTS
Z. PHYSIK. CHEM.IFRANKFURT)48(3-4I,129-44(1966)GER
CA-65-1433 B
KRAMSJ66EOT KRAMER SJ
EFFECT OF THE EXTERNAL SURFACE ON THE REACTION RATE AND
SELECTIVITY OF ISOTHERMAL CATALYST PARTICLES
J. CATALYSIS 5(1),190-2(1966)ENG. CA-64-11913 B
KRASJH55EFW KRASUK JH
EFFECTIVENESS FACTORS WITH SURFACE DIFFUSION
INO.ENG.CHEM.FUNDAMENTALS 4(1).102-611955)ENG CA-62-5930 H
KRASJH65EFS KRASUK JH SMITH JM
EFFECTIVENESS FACTORS WITH SURFACE DIFFUSION
IND.ENG. CHEM.FUNDAMENTALS 4iDF 102-611965)ENG CA-62-5930 H
KRAUA 55IIC KRAUSE A
INVESTIGATIONS IN CATALYSIS
PRZEMYSL CHEM. 34,11-13(19551 CA-53-838 B
KRAUA 62CAM KRAUSE A
CHEHISORPTtON AND MECHANISM OF CATALYTIC REACTIONS ON OXIDE
CATALYSTS
OESTERR. CHEMIKERrZTG 63.49-51(1962) CA-56-12355 A
KRAUA 62RTT KRAUSE A
RAISING THE THERMAL RESISTIVITY OF THE V205 CATALYST BY
ALUMINUM-HYDROXIDE
ROCZN1KI CHEM. 36.717-19(1962) CA--58-960 D
KRAUA 63COA KRAUSE A
CHEMISORPT10N OESORPTION AND MECHANISMS OF CATALYTIC
REACTIONS ON METAL CATALYSTS
OESTERR.CHEMIKER-ZTG. 64(5),142-4(1963) CA-59-8157 E
KRAUA 64TDO KRAUSE A ZIELINSKI S
THE DETECTION OF PREMATURE GRADUAL CHANGES OF THE SURFACE
LAYER OF SOL in BODIES AS ILLUSTRATED BY V205
MONATSH 9«>( 21. 598-9( 19641 CA-61-7750 E
KRAUA 67HAL KRAUSE A
HIGH AND LOW-TEMPERATURE MECHANISMS OF CATALYTIC OXIDATION
REACTIONS ON SEMICONDUCTING OXIDES
OESTERR. CHEM.-ZTG. 6814),126-7(19671GER. CA-67-26105 W
ROCZNIKI CHEM. 39(10 I,1491-7(1965IPOL CA-64-B970G
209
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KRAUA 67ROO KRAUSE A
REACTIONS OF OXIDE CATALYSTS WHOSE OXYGEN EXCHANGES WITH THE
SUBSTRATE OXYGEN AND DEFINITION OF ACTIVE METAL OXIDE
OESTERR. CHEM.-ZIG 68(7),219-2011967IGER CA-68-53714 W
KPAUHH68SOR KRAUSE HH
LEVY A
REID HT
SULFUR7QXIDE REACTIONS RADIOACTIVE.SULFUR AND NICRDPROBE
KREJE 654ER
KRISSR66RSD
KRIZM 65SGR
KRUEM 67AEM
STUDIES OF
J.FNG.POWER 90(1)
KREJAR E
:~ EXCHANGE
CHEM. PRUMYSL I5(2)i
DEPOSITS
38-44119681ENG CA-68-80802 E
-9I1965ICZECH CA-62-11183G
AN I ON-EXCHANGE. RESINS AS . SgRBENTS_OF_ SULFURrpI OXIDE
KRISHNAN SR
REMOVAL OF SULFUR-DIOXIDE FROM STACK GASES OF
SULFURIC-ACID PLANTS
TRCHNOLOGYISINORI l.SPEC.ISSUE 31 41 , 51-311 966IENG
CA-68-H97010
KRIZ M
SULFUR-OXIDES REMOVAL FROM FLUE-GASES
SKLAR KERAM. 1 5( 12) , 374-6( 1965ICZECH CA-64-17079 B
KRUEL M JUENTGEN H
ALKALINE EARTH METAL COMBINATION WITH S02 OF FLUE-GAS
IN A FLUE OUST CLOUD
CHEM.-ING.-TECH. 39(9/101,607-13119671 CA-67-76094 N
KRUEM 67SDR KRUEL M
JUENTGEN H
ORATWA H
SULFUR-DIOXIDE REMOVAL OF FLUE-GASES
U.S. 3,345,125 (CL. 22-31.OCT.3,1967 GER. APPL. NOV. 13.1965
CA-68-IRI-15B52 G
KRUME 41VCM KRUMMENACHER E HECKER A
VANADIUM CATALYTIC MASSES IN MANUFACTURE OF SULFUR IC-AC10
HELV.CHIM. ACTA 24,71-911941) CA-37-2145-7
KUBEJ 67ECO KUBEC J SAROCH V
EQUIPMENT TO CHARGE AND DISCHARGE CATALYST PACKING (IF
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CZECH.121,727 ICL.B 01J),JAN.15,1967.APPL.AUG.7,1965
CA-6*-(P)-23023 C
KUBOH 610PC KUROTA H NAMKOONG S AKEHATA T
SHINDO M
OPTIMUM PROCESS CONDITIONS FOR A COMPLETELY MIXED MULTISTAGE
REACTOR
CAN. J.CHEM. ENGR.39,64-6(1961) CA-55-13944-B
KUBOT 54CAO KUBO T TANIGUCHI M KATAOKA K
CATALYTIC ACTIVITY OF VANADIUM-PENTOXIDE CATALYST ON
TITANIUM-DIOXIDE CARRIER AND ITS MEMBRANE POTENTIAL
J.CHEM.SOC.JAPAN, IND.CHEM.SECT.57,705-7(1954) CA-49-10717 G
KUBOT 57EOX KUBO T
TANIGUCHI M
EFFECTS OF X-RAY IRRADIATION ON THE OXIDATION OF
SULFUR-DIOXIDE BY VANAOIA-TITANIA CATALYSTS
KOGYO KAGAKU ZASSHI 60,1225-8(1957) CA-53-13798 C
KUCZH 59ATI KUCZYNSKI M ROSOCHOUICZ J
ATTEMPTS TO INCREASE THE THERMAL RESISTANCE OF THE
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ROCZIKI CHEM. 33,479-92(1959) CA-53-20624 G
KUCZH
KUCZW
KUEFA
KUESU
61CCF
63CFS
62SSW
65TOF
KUCZYNSKI W WESOLOWSKI J
CONTACT CATALYST FOR SULFUR-DIOXIDE OXIDATION
POL.45,274,NOV.16.1961,APPL.WAR.22,1961 CA-57-1Pl-l1907 A
KUCZYNSKI M WESOLOWSKI J
CATALYST FOR S02 OXIDATION
PREHYSL.CHEM. 42(61,290-1(1963) CA-59-7019 F
KUEFFER A
THE SOLUBILITY OF S02 IN WATER
PAPIR CELULOSA 17,125-6(19621 CA-61-6460 D
KUHOH 590CF KUBOTA H
AKEHATA T
SH
IC
HINDO
OPTIMUM CONDITIONS FOR GAS-SOLID CATALYTIC REACTION PROCESS
IN A FIXED-BED
KAGAKU KOGAKU 29,506-12(1959) CA-53-I8560 B
KUBOH 59TRC1 KUBOTA H ISHIZAWA M SHINOO M
THE RATE OF OXIDATION OF S12 WITH INDUSTRIAL VANADIUM
CATALYST
RYUSAN 12.243-5K 19S9I CA-54-2562P C
KUBOH 60DOF KUBOTA H _ . . .
DESIGN OF FIXED-BED TYPE CONVERTER FOK S02 OXIDATION
AKEHATA T
TYPE CONVE _
RYUSAN 11, 160- 3(1960) CA-55-16924 C
SHINOn N
KUESTERS W
TREATMENT OF FLUE-GAS
METH.APPL.6,607,238 (CL. B 010)IJAN.10.1967.GER.APPL.JULY 9
1965 CA-r66-(P)-118592 K
KUEZU 62CCS KUEZYNSKI W KANIA W
CHROMIC CATALYSTS SUPPORTED ON AL203
POZNAN.TOWARZ.PRZVJACIOL NAUK.WYDZIAL MAT.-PRZYROD.PRACE
KOHISJI MAT.-PRZVROO. 9, NO.3,79-25U962ICA-59-2207 G
KUEZW 6600S KUEZYNSKI W KANIA W
OXIDATION OF SULFUR-DIOXIDE ON NON MODIFIED CHROMIUM-ALUMINA
CATALYSTS
PRZEM.CHEM. 45( 121.659-621 1966IPOL CA-66-10B674 Z
KUHL 3600S KUHLHANN
HXIOATION OF SULFUR-DIOXIDE
FR. 895, 605. NOV. 25, 1936 CA-31-JP)-4462-9
KUHL 38ST KUHLMANN
SULFUR-TRIOXIDE
GER.662.445.JULY 13. 1938ICL. 121 24) CA-32-( P)-7687-8
212
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KUHL 63SO
KUHLMANN
SULFUR-DIOXIDE
FR. 1,381(578 (CL.C 018) DEC.11,164,APPL.OCT.30,1963
CA-62-(P|-10III2 6
KUNIN TI
QXIDATinN OF SULFUR-DIOXIDE BY NITROSE IN SULFURIC-ACID
KHIN.PROM.1946,NO.12,8-9 CA-41-4277I
KUNIN TI SOLOV'EV BI
ACTIVITY OF THERMALLY STABLE VANADIUM CATALYSTS FOR THE
OXIDATION OF SULFUR-DIOXIDE
1963 76i-B4 CA-60-4B43 F
KUO CW HF. I J
TRACER METHOD FOR EVALUATING CATALYTIC DATA
A. I. CH. E. J. 13(41,657-6211967IENG CA-67-67969Z
KURGANOV VM GONSALES A KARAVAEV NM
THE LIMITING CONDITIONS OF THE EXISTENCE OF A GRANULAR
CATALYST BED
NEFTEPERERERABOTKA I NEFTEKHIM..NAUCHN.-TEKHN.SB.1965(12 I
21-51 RUSSI CA-65-16690 H
KURGVM66CPM KURGANOV VM GONSALES A KARAVAEV NM
CERTAIN PRINCIPLES OF THE MOTION OF CATALYST PARTICLES IN
INDUSTRIAL VERTICAL PNEUMATIC CONVEYING
KHIM. I TEKHNOL. TOPLIV. I MASEL 11(2 I,3-7(19661RUSS
I KUNIT14600S
KUNITI63AOT
KUO CH67TME
KURGVM65TLC
CA-65-3374 C
SIGOV SA
SEMENOVA GI
KURINP40TCP KURIN NO
VtlROB'EVA MM
THE CATALYTIC PROPERTIES OF NONPLATINIJM CATALYSTS IN THE
OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIOXIOE THE
ACTIVITY OF IRON-COP">F«.CATALYSTS
IZVEST. TOHSKOGO INO. INST. 60,NO.3,79-129(19*01 KHIM.
REFERAT. ZHUR. 1940,NO. 9,61-2 CA-37-2145-1
KURINP56ACO KURIN NP RUOYUK NT
THE ACTIVITY OF CHRtlMIUM-OXIOE STANNIC-OXIDE CATALYSTS FOR
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IZVEST. TOMSK. POLITEKH. INST. 83,163-74(1956) REFERAT ZHUR
KHIM 1956.ABSTR. NO. 67935. CA-53-21104 A
KURINP56CFO KURIN NP FIGUROVSKAYA NP
CONTACT PROPERTIES OF CHROMIUM-QXinE-STANNI C-OXI OE CATALYSTS
FOR THE OXIDATION OF SU2 TO S03
IZVEST. TOMSK. POLITEKH.INST.83,210-39119561ARSTR.NO.67914
CA-53-21104 C
KURPC 64ROP
KUZIVA65DCF
NAUNOORF H
KURPJUN C .
RECOVERY OF PLATINU"! FROM CONSUMEn PLATINUM CATALYSTS
CHfM.TECH.(BERLIN) 16(7),392-611964IGFR.CA-62-253 E
KUZIN VA
DESIGN CALCULATIONS FOR PROCESSES IN FIXED-BEDS AND
FLUIDIZEO-BEDS OF CATALYST
VSES.KUNF.KHIM.REAKTORAM 3,471-9(19651RUSS CA-6R-88551
213
KUZMIN36TOT KUZ*MINYKH IN TURKHAN EY ARKHIPOVA MS
THEORY OF THE CHAMBER-PROCESS MECHANISM AND THE KINETICS OF
OXIDATION OF S02 RY NO2 IN THE GAS PHASE
Z.ANnRG.ALLGEM.CHEM.226,3IO-20(19361 CA-30-4275
KUZMIN6100S
KUZMIN64POS
KUZNIE66PIG KUZNETSOV IE
KUZ'NINYKH IN SALTANOVA VP
OXIDATION OF SULFUR-DIOXIDE IN A FLUI01 ZED-BED CATALYST
TR.MOSK.KHIH.-TEKHNOL.INST. 1961,NO.35,125-9 CA-57-3247 C
KUZ'MINYKH IN
PRODUCT ION_OF SULFUR IC-AC ID
USSR.
5 JULY 22,1964 CA-61-(PI-14225 C APPL. OCT.13,1947
GANZ SN
PURIFICATION OF INDUSTRIAL GASES FROM SULFUR-DIOXIDE
IZV. VYSSHIKH VCHEBN. ZAVEOENII, KHIM. I KHIM. TECKHNOL.
9( ll,89-93( 1966IRUSS CA-65-879F
KUZNVS6400T KUZNETSOV VS
ORIGIN OF THE COMPENSATION EFFECT IN CHEMICAL REACTIONS
OCCUR ING ON THE SURFACE OF SEMICONDUCTOR CATALYSTS
KINETIKA I KATALIZ 51 2 I , 277-831 1964ICA-6I-3728 H
LABUGV59AFC LABUTIN GV VERESHCHAGIN f°
APPARATUS FOR CONTACT OXIDATION OF SULFUR-DIOXIDE WITH A
FLUIDIZED-BEO OF CATALYST
USSR. 117,104 JAN. 29,1959 CA-53-(P»-20723 E
LADNHR63FRT LAONER UR PANKHURST KS
FORMATION OF SULFUR-TRIOXIDE APPLICATION OF INFRARED
SPECTROMETRY TO FUNDAMENTAL STUDIES
MECH. CORROSION FUEL IMPURI TIES.PROC. INTERN.CONF. MARCHHOOD
HAMPSHIRE.ENGL. 1963,195-2 CA-62-9792 E
LAMBB 25CFO LAMBERT B
CATALYSTS FOR OXIDATION REACTIONS SUCH AS OXIDATION OF
SULFUR-DIOXIDE
U.S.1,814.515 JULY 14 CA-25-(PI-5258-3
LAMRB 27CFO LAMBERT.! AND NATIONAL PROCESSES,LT
LAMMC 66RNO
CATALYSTS FOR OXIDIZING SULFUR-DIOXIDE
BRIT.301,853,SEPT.6, 1927 CA-23-1PI-4306
0.
!PE
LAMM C SCHUMANN KLAUSS J
REMOVAL OF NITROGEN-OXIDE CONTAINING SULFURIC-ACID FUMES
GER.(EAST) 50,584 (CL. C OIL),OCT. 5, 1 966 , APPL. APR I L 17.1965
CA-66-(P)-96985M
LAMMC 66SAC LAMM C SCHUMANN H KLAUSS J
SULFURIC-ACID BY CONTACT PROCESS
GER.
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LANGO 6400A
LASTYV6600S
LANGHEIN D
OPTIMIZATION OF AN ADIABATIC STAGE REACTOR
DECHEMA.MONOGRAPH. 50(376-884),35-50(1964) CA-61-10336B
LASTOCHKIN YV
RUMYANTSEVA ES
MUKHLENOV IP
BONDARCHUK TP
LESOKHIN IG
OXIDATION OF S02 IN AM APPARATUS WITH A FLUIOIZED-BED OF FE-
OX^DE CATALYST DURING H2S04 PRODUCTI ON. BY THE CONTACT
KHIMiPROM.42(61,445-81 1966IRUSS CA-65-19553 0
LAVOKP64KOS LAVORSKII KP ROSENTHAL AL
KINETICS OF SORPTION AND OF THE CHEMICAL REACTION ON A
UNIFORM-SURFACE CATALYST IN A FLUID!ZED BED INVOLVING
COMRLETF. -INTERMIXING OF. PARTICLES AND OF THE GAS
KINETIKA 'I KATALIZ 7( 11 , 15 l-6< 1966IRUSS CA-64-15037 E
LAWLWC USD LAWLER WC
USE OF A SULFUR-DIOXIDE SCRUBBING SYSTEM IN AIR POLLUTION
CONTROL
PROBLEMS AND CONTROL OF AIR-POLLITUON 1955-222-2* CA-50-2505
LE BA 67AUW LE BRAS A
ACTION OF ULTRASONIC WAVES ON CHEMICAL AND PHYSICOCHEMICAL
REV. CHIM. MINER 411).2B3-315(1967IFR..CA-66-41032 T
LEE FA66THF LEE FA WIESENTAHL P
TERRACED HEATERS FOR CATALYSTS FILLED TUBES
US.3^230 jOSjMCL 23-277)JAN. 18, 1966,APPL.NOV.28 1«J61
LEE GK67EFC LEE GK FRIEDRICH FD MITCHELL ER
EFFECT OF FUEL CHARACTERISTICS AND EXCESS COMBUSTION AIR
ON SULFURIC-ACIO FORMATION IN A PULVERIZED COAL-FIRED
. J. INST. FUEL 40(320),397-405( 1967IENG CA-67-110377 A
LEF KY63COA LEE KY ' . ARIS R
CONTROL OF A COLO SHOT ADIABATIC
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BED REACTOR WITH A
.IND.ENG.CHEM. PROCESS DESIGN DEVELOP ?(4),306-911963)
CA-59-9611 F
LEE KY630AB LEE KY ARIS R
OPTIMAL ADIABATIC BED REACTORS FOR SULFUR-DIOXIDE WITH COLD
SHOT COOLING
INO.ENG.CHEM..PROCESS DESIGN OEVELOP.2(41,300-611963).
CA-59-^9611 E
LF.E VJ64TCT LEE VJ
THE CHARGE TRANSFER THEORY DF GAS-SURFACE INTERACTIONS AND
HETEROGENEOUS CATALYSIS (IN SEMICONDUCTORS
UNIV. MICROFILMSIANN ARBOR,MICHI ORDER NO.64-6711
DISSERTATION ABSTR 241121,5274-511964)CA-61-8937 H
LEITW 67POA ^EVENT/ION QF A,R pOLLUTION A PRESSING DEMAND FOR CHEMISTRY
ALLG1? PRAKT!!VCHEM.18(8),411-12,417(1967)GER CA-67-119998 E
LEKAKE66BMS LEKANDER KE
BLEACHED MAGNESIUM-SUL FI TE PULP
NORSK SKOGIND. 20(6),224-
LEO JG6 REHOVINGJIRON FROM DEACTIVATED OIL TREATMENT CATALYSTS
U.S. 3,206,413 (CL.252-411I.SEPT.14,1965,APPL.NOV. 23,1962
CA-63-(P)-14617 H
3111966) (SHED.I CA-65-18827 G
LEVIGR27DAO LEV! GR
IN THE'CATALYSTS" OF SULFURTC-ANHYORiDE
opRHODIUM AND OF IRIOIUN UPON PLATINUM
DELETERIOUS ACTIO
IN THE CATALVSI
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VANADIUM MODIFIED CRYSTALLINE ALUMINOSILI
PROPERTIES
EVICH LN ERMOLENKO NF
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LEVVA 67ISO
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NFLUENCE OF EXTERNAL DIFFUSION INHIBITION ON THE
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"- *N~ IN CORROSION AND DEPOSITS
LEVY A _ _
SULFUR CHEMISTRY AND ITS ROLE ...
J.ENG.POWER 85(3),229-34(19631 CA-59-8518 H
LEVY A MERRYMAN EL
INTERACTIONS IN SULFUR-OXIDE IRON-OXIDE SYSTEMS
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HEAT REMOVAL FROM FLUIOIZED SOLID REACTOR BEDS
US.2,474,583 JUNE 28,1949 CA-43-(P)-6478-C
INFLUENCE OF REACTION!RATEDON OPERATING CONDITIONS IN THE
CONTACT SULFURIC-ACIO MANUFACTURE
INO.ENG.CHEM. 17.593-81 19251 CA-19-2111
WK
_ ON TH
CONDITION
INO. ENG.CHEM
INFLUENCE OF REACTION RATE ON OPERATING
IN SULFURIC-ACID MANUFACTURE
18 24311926) CA-20-971
LE2HKAMAOO LEZHNEVA KA BORISOVA Tl SLIN'KO MG
ANODIC OXIDATION OF SULFUR-DIOXIDE ON GOLD AND PLATINUM-GOLD
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OPTIMIZATION OF THE .OXJDATI ONQF SULFUR-DIOXIDE
LIBELM64ADO LIBERZDN LH
AUTOMATIC OPTIMIZATION OF THE OXIDATION OF SULF_. _ _-
TR.NAUCHN.-ISSLED.INST.Pg_UDOBR.| INSEKTOFUNGITSIDAM N0.205
104-101 19641RUSS CA-64-7722 H
LISLES65DOS LISLE ES
LIU SL67NSD
„ SENSENBAUGH JD
DETERMINATION OF SO2 AND ACID DEW POINT IN FLUE-GASES
COMBUSTION 36(71,12-1611965IENG CA-62-15952 G
NUMERICAL SOLUTION OF TWO-POINT ROUNDRY VALUE PROBLEM VALUE
PROBLEMS IN SIMULTANEOUS SECOND-ORDER NONLINEAR ORDINARY
DIFFERENTIAL EQUATIONS
CHEM. ENG. SCI. 22(61,87l-81(1967)ENG CA-67-55531 N
LODG 66EME LODGE-COTTRELL LTD
ELECTROPRECIPITATION METHOD AND EQUIPMENT
FR. 1,445.982 ICL. 8 910J.JUI.Y 15,1966 BRIT APPl.SEPT. 1 , 1964
CA-66-(PI-47841 C
LOEBE 61SAC
LOWRGC58CSI
LUOWJM67COS
LUOWS 68APV
LOEBL E
SEMICONDUCTORS AND CATALYSIS
TRANS. N.Y. ACAD. SC I .23,491-4(1961 I CA-61-10154 H
HEPPENSTALL
" ~ 'ACTURE OF SULFURIC-ACIO BY
CA-67-46916 0
CONVERSION STAGE IN THE MANUF
CONTACT PROCESS
BRIT.CHEM.ENG.3,252-7,310-151 1958) CA-52-149B9 I
LUDWIG JH SPAITE PW
CONTROL OF SULFUR-OXIDE POLLUTION
CHEM. ENG.PROGR. 631 61 , 82-61 1967(ENG
LUDWIG S
ANTIPOLLUTION PROCESS USES ABSORBENT TO REMOVE
SULFUR-DIOXIDE FROM FLUE-GASES
CHEM. ENG.(N.Y.) 75(31, 70-2 (I9A8IENG. CA-68-62466U
BUSHMHKIN IN
RUISAKOV MV
LUKYPM33COO LUK'YANOV PM
MOLKENTIN IR
CONTACT OXIDATION OF SULFUR-DIOXIDE TO SULFUR-TRIRXIDE UNDER
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J. APPLIED CHEM. (U.S. S.1?. ) 6,772-fl4{ I 9331 . CA-28-4181-4
LUPAK 66PEV LUPAOER K
PPOCESS FOR EXTRACTION OF VALUABLE PRODUCTS FROM SCHISTS
AND OTHER BITUMINOUS FERRUNGINOUS AND SULFURDUS SEDIMENTS
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AKTIEBOLAG ATOMENERGI FR. 1,43 3,73* (CL. C 048, C 22BI .
APRIL 1,1966, APPL.APRIL 2ft,1965 CA-66-1PI-12597A
LUO'JF 67TAO LUQUET F
THE APPLICATION OF A GRADIENT METHOD TO THE OPTIMIZATION OF
ADIABATIC MULTISTAGE CATALYTIC REACTORS
CHIM.IND.,GENIE.CHIM.97(61,932-611967IFR CA-67-5542P A
LUSSO 670AC
LUSSD 68SOB
MACAJ 67AFD
LUSS 0 AMUNDSON NR
ON A CONJECTURE OF ARIS PROOF AND REMARKS
A.I.CH.E J.13(41,759-63(1967IENG CA-67-74953 T
_ AMUNDSON NR
STABILITY OF BATCH CATALYTIC FLUIDI ZED-BEDS
LUSS 0
STABILI. . _. . ..
A.I.CH.E. J.14(21 211-21 (I968IENG CA-68-88580 B
MACAK J MALECHA J
APPARATUS FOR FAST DETERMINATION OF THE ACTIVITY OF
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CHEM. LISTY 61 ( 3),368-7711967)CZECH CA-67-15308 P
MACKJ 65IFB HACKLEY J
IMPROVEMENTS IN FIXED-BED CATALYST OPERATIONS
BELG. 656,067.MAY 20,1965 BRIT.APPL.NOV.21,1963
CA-65-IP)-14494 G
MAEOS 51HTI MAEDA S KAWAZOE K
HEAT TRANSFER IN GRANULAR BEDS TEMPERATUR DISTRIBUTION
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CHEM.ENG.(JAPAN)15,312-16(1951) CA-46-7377-C
MAGYM 64KFR MAGYAR M
KINETICS FOR REACTIONS OF HETEROGENEOUS CATALYSIS
KINETIKA I KATALIZ 5( 5 ) ,831,41< 1964 IRUSS CA-62-59D
MAHABK640AS MAHAT BK BOSE NK
OXIDATION OF AMMONIACAL SULFUR-DIOXIDE SOLUTION WITH
OXYGEN IN A STIRRED AUTOCLAVE
INDIAN CHEM. E "~
ENGR. 6(3) 57-64(1964) CA-62-14169-D
MAHASD32TOO MAHANT SO
MAISJE27FOS
THE OXIDATION OF SULFUR-DIOXIDE IN A ELECTRODELESS DISCHARGE
J.INDIAN CHEM.SOC. 9,417-22(19321 CA-27-1829-3
MAISIN JE
FORMATION OF SULFUR-TRIDXIDE UNDER THE ACTION OF ALPHA
PARTICLES
ANN.SOC.SCI BRUXELLES 47R,I,172-7(19271 CA-Z2-2722-5
MAKIS 57TMO MAKISHIMA S
THE MECHANISM OF SOLID CATALYSTS WITH SPECIAL REFERENCES TO
SEMICONDUCTOR CATALYSTS
KOGYO KAGAKU ZASSHI 60,1230-3(1957) CA-53-13753 F
MALAJ 35SGC MALAN J MALAN GH
SILICA-GEL CATALYSTS
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MALIIK6600C HAL IMA IK
DEVELOPMENT OF CONCEPTS DN REACTION MECHANISM OF
SULFURIC-ACID PRODUCTION
RAZV, PREDSTAVLENII (1BL. KI NET. .KATAL.REAKT. SPOSOBNOSTI
AKAOfNAUK SSSK,INST.ISTDR.ESTESTVnZN.TEKH.1966,123-49(RUSS I
CA-67-66077 V
MALKVI640SA MALKIMAN VI
OPTIMUM SHAPES AND SIZES OF ELEMENTS OF A VANADIUM CATALYST
FOR THE PRODUCTION OF CONTACT H2S04
NAUCHN.OSNOVY PODBORA I PROIZV. KATALIZATOROViAKAD.NAUK SSSR
SB.OTD. 1964, I 88-92 RUSS CA-63-7925 P
NALLFS PCA MALLETTE FS
PROBLEMS AND CONTROL OF AIR POLLUTION
REINHOLO PUB. CORP.,NEW YORK.N.Y (143-5411953 CA-50-5205F
MALLHC67FBO MALL ISDN HC RANDALL GA SEAVER PH
ROUSSEAU WC EGBERT RB
FLUIDIZED-BED DIFFUSION
U.S. 3,298,793 ICL. 23-888) JAN 17,1967,APPL.APRIL 4,1963
CA-66-CRI-77480 B
MALTR 61ROS MALTBY R
PRODUCTION nf SUFURIC-ACID AND OXIDE FROM GAS PURIFICATION
YEABBOOK COKE OVEN MGRS.«ASSOC.,1963,331-55 CA-61-6823 A
PASEK J
HORAK J
MAMUP 67HAH MtMULA P
KONDELIK P
HEAT AND MASS TRANSFER IN HETEROGENEOUS CATALYSIS VII EFFECT
OF CATALYST HEAT CONDUCTIVITY ON THE OVERALL HEAT
TRANSFER COEFFICIENT IN A PACKED TUBE
CHEM.PRUM. 17(8).416-24( 1967ICZECH CA-67-( Pl-l 18554 V
MANDBG66COS HANDEL IK BG
CONVERSION OF
US.-3,282,645
MANTR 67SAC MANTEUFEL R
SULFURIC-ACIO CONCENTRATION PROCESS
U.S. 3,294,650 (CL.203-221, DEC.27,1966 APPL.AUG 13,1962
CA-67-(P)-92421 X
MAREM 68MQC MAREK M HLAVACEK V
MODELLING OF CHEMICAL REACTORS VI. HEAT AND MASS TRANSFER
SULFUR-DIOXIDE WITH LOW IGNITION CATALYSTS
(CL.23-1761,NOV.l,1966 CA-66-(PI-4550 S
IN A POROUS CATALYST PARTICLE THE MULTIPLICITY OF SOLUTION
FOR THE CASE OF AN EXOTHERMIC ZERO-ORDER REACTION
COLLECT. CZECH.CHEM. CHEN. COMMUN.13(2),506-17(1968IENG
CA-68-705H8 A
MARSJM67GVO "ARSANS JM
GENERAL MECHANISM OF CATALYTIC REACTIONS
AFINIDAD 241 250 ) , 157-651 19A7)SPAN.
PARSP 54QCO MARS P KREVELEN DW
OXIDATION CARRIED OUT BY MEANS OF VANADIUM-OXIDE CATALYSTS
CHEM. ENG.SCI. T. SPEC. SUPPL.,41-5«>| 1054) CA-50-92II
MAESSEN JGH
THE MECHANISM OF THE OXIDATION
MARSP 64TMO MARS P __
~HE MECHANISM OF THE OXIDATION OF SULFUR-DIOXIDE ON
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PROC.INTERN.CONGR.CATALYSIS,3RD ANS"
DISCUSSION 27B-8KPUB.1965)
1STERDAM,1964.1 266-79
MARSP 68TMA
THE MECHANISM AND THE KINETICS OF SULFUR-DIOXIDE OXIDATION
ON CATALYSTS CONTAINING VANADIUM AND ALKALI OXIDES
J.CATAL. 10( 11,1-121 1968IENG
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CATALYTIC OXIDATIONS IN THE GAS PHASE
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CA-42-8058-H
MARTTC66CSP MARTIN TC
CONCENTRATION OF SULFURIC OR PHOSPHORIC-ACID
-' " 159-15),DEC 6,1966.APPL. NOV. 13,1963
U.S. 3.289,733 (CL.
CA-66-m-3<»427 G
MASAS 66PFC
MATAVL67PSA
MASAMUNE S SMITH JM
PERFORMANCE OF FOULED CATALYST PEL
A.I.CH.E. J. 12<2).334-941 1966)ENG
iA-64-15038 E
MATASOV VL
PURIFICATION OF SULFURIC-ACID IRON CONTAINING WASHING
BVULL.TEKH.-EKON. INFORM.,COS.NAUCH-ISSLEO.INST. NAUCH TEKH.
INFORM. 20111I,3-5(1967)RUSS
MAUSF 67SCH MAUSS F
PERTHU1S
SULFURIC .CORROSION IN HOT WATER BOILERS
REV. INST. FR. PETROL ANN.COMBUST. LIOUIDES 22(61,1053-80
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MAXIMS33COO MAXIM MS
CATALYTIC OXIDATION OF SULFUR-DIOXIDE
US. 1,947,829. OCT.25 CA-28-7442-2
MAXTEB28IOA MAXTEO EB DUNSBY AN
INFLUENCE OF ARSENIC ON THE CATALYTIC ACTIVITY OF PLATINUM
FOR THE OXIDATION OF SULFUR-DIOXIDE
J.CHEM.SOC.1928,1600-3 CA-22-4332-9
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CATALYTIC OXIDATION OF SULFUR-DIOXIDE IN THE PRESENCE OF
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SELECTION OF CAST
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RESISTANT TO CORROSION BY
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220
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MCILAE66IFB MCILKINNEY AE DSRERG GL
IMPROVEMENTS IN A FLUIOIZED-BED PROCESS
~ " '•- " B 01J),FER.2.1966 U. S.APPL.OCT.26,1961
META 64MOS
BRIT. 1,019,236 (CL.
CA-64-IP)-l5419 H
MEAJEP67PSW HEAUX EP
PARTICIPATE SOLIDS WITHDRAWAL METHOD
U.S. 3,336,217 (CL.206-143).AUG. 15,1967,APPL.JULY 15,1965
U.3. S.330,£11 III
CA-67-IPI-92371 f
MEISHPfrOC.TU MEISSER HP
MELLRA66GAA
SCHORA FC
GRAPHICAL TECHNIQUES FOR ADIABATIC STAGED SYSTEMS
TRANS. AIME 460-8119621 CA-57-5750 E
ME RMS 66BTA
MERRHF27TOG
MERTE 47FHC
MESAS 66POF
META 37VCF
META 52POS
META 62ASD
"ELLROY RA MARKANT HP
GAS ABSORPTION APPARATUS
U.S. 3,284,435 (CL.261-151 I.NOV.8.1966.APPL. AUG.13,1962
4NO NOV. 19,1965 CA-66-IP )-7747] Z
MERMERSKI S ZHELEVA A
BEHAVIOR OF TOMBAC ALLOY IN SOME CORROSIVE MEDIA
KHIM. IND.(SOF1AI 38(71,296-3021 1966IBULG
MERRIAM HF
TREATMENT OF GAS FOR SULFURIC-ANHYDRIDE MANUFACTURE
CAN. 334,508,AUG.1,1933 CA-27-(P1-5488-3
MERTENS E
FLUIDIZED HETEROGENEOUS CATALYSIS BY THE METHOD OF CURRENTS
J.CHIM.PMYS.47,286-8 CA-44-7637 E
SMITH JM
Li° CATALYST PELLETS.
•ASAMUNE S
PERFORMANCE OF FOULED _ .
A.I.CH.E J 12(21,384-94(1966) ENG CA-64-15038 E
METALLGESELLSCHAFT
VANADIUM CATALYSTS FOR OXIDIZING SULFUR-DIOXIDE
GER. 649,401,AUG.23.1937.(CL.12G.4.01) CA-32-1P)-1062
METALLGESELLSCHAFT
PRODUCTION OF SULFUR-TRIOXIDE BY THE CONTACT PROCESS
BRIT. 672,636,MAV 21,1952 CA-46-(PI-U608 0
METALLGESELLSCHAFT
ABSORPTION OF SULFUR-DIOXIDE FROM GAS
METALLGESELLSCHAFT A.-G- GER. 1,176,101 (CL. C 01B) AUG. 20
1964.APPL. SEPT. 4,1962 CA-61-(Pl-l1656D
MFTA 64CTC METALLGESELLSCHAFT
CARBON-TYPE CATALYST FOR THE CONVERSION OF SULFUR-DIOXIDE
TO SULFUR-TRIOXIDE
GER. 1,176,621 ICL. C CIB) AUG 27,1964, APPL. DEC. 1,1962
CA-62-(P)-M57 F
META 64IPR METALLGESELLSCHAFT
INCREASED PRECIPITATION RATE OF ELECTROSTATIC SEPARATORS
METALLGESELLSCHAFT A.G. FR. 1,448,415 (CL. B 01DI.AUG 5,1966
GER. APPL. SEPT. SEPT. 18,1964, CA-66-IPI-79341 F
META
METT
METALLGESELLSCHAFT
MANUFACTURE OF SULFUR-TRIOXIDE
FR. 1,370,911(CL C 01B) AUG.28.1964 GER.APPL.AUG.16,1962
CA-62-(P)-B714 C
META 64SAS METALLGESELLSCHAFT
SULFURIC-ACID FROM SULFUR-DIOXIDE CONTAINING GASES
NETH. APPL. 6,405,596 (CL.C 018).NOV.23,1964 GER. APPL.
MAY 21,1963 ADDN. TO NETH. 270,297 CA-62-(P)-87060
META 64STF METALLGESELLSCHAFT
SULFUR-TRIOXIDE FROM GAS LOW IN SULFUR-DIOXIDE CONTENT
GER. 1. 177,117(CL.C.01BISEPT 3,1964 APPL.NOV. 16,1962
CA-61-(P)-11656 E
META 65TBC METALLGESELLSCHAFT
THERMALLY BALANCED CATALYTIC OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-THICK IDE AND SULFURIC-ACID
GER. 1.186,838(CL.C 018 I.FEB.11,1965.APPL JUNE 22,1963
CA-62-(PI-1456 E
MFTA 66HAC METALLGESELLSCHAFT
66POS
62MBC
HEATING AND COOLING OF SUL FUR IC-AC I D CONTACT CONVERTERS
GER. 1.210.422 (CL C OIR) .FEB. 10. 1966 APPL. MAR. 1 ,1963
CA-64-IPI-12240 F
METALLGESELLSCHAFT
PRODUCTION (IF SULFUR-TR IOX IDE AND SULFURIC-ACI D
BRIT. 1,039,349(CL.C 01B I , AUG. 17, 1966 CA-65-( P ) -11 836 C
METALLGESELLSCHAFT
C
6
l
METALLGESELLSCHAFT
MULTIPLE-BED CATALYTIC REACTORS
GER. 1,129.936 (CL. 12DMAY 24, 1962 .APPL. SEPT. 8, 1960
CA-57-(PI-576l F
2,1965 GER APPL. OCT. 17,1960
PRODUCTION OF SULFURIC-ACID
BRIT.994,070 ICL. C Olfl I.JUNE
CA-63-(P 1-3926 A
METT 65STO METALLGESELLSCHAFT
SULFUR-TRIOXIDE OF SULFURIC-AC10
NETH. APPL. 6,508,068(CL.C 01BI DEC.24,1965 CA-64-(P)-170978
METT 66CVG METALLGESELLSCHAFT
CATALYTIC VAPOR-PHASE GAS CLEANING
FR.1,449,164 (CL.B 01JI AUG.12,1966 CA-67-(PI-66070 N
METT 66MPF METALLGESELLSCHAFT
MULTISTAGE PURIFICATION OF FLUE-GASES
NETH. APPL. 6.516,703 (CL . C. 01BI.JULY 4,1966
CA-65-IPI-1B202 E
METT 66SAS METALLGESELLSCHAFT
S03 AND SULFUR IC-ACIO RV CATALYTIC CONVERSION OF CASES
CONTAINING 502
NFTH. APPL. 6, SO?
.65KCL. C OIR) JAN.10.1966 CA-64-( P|-1 7097C
222
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61
MFTTAL65PSA HETALLGESCLLSCHAFT
PRODUCTION OF SULFURIC-ACID
BRIT.994(070 (CL.
CA-63-(P)-3926 A
C OlBifJUNE 2,1965 GER. APPL. OCT.17,1960
HEZAR 66SPE HEZAKI R KITTRELL JR
SOME PARAMETER ESTIMATION CONSIDERATIONS FOR HETEROGENEOUS
KINETIC MODELS
KAGAKU.ROGAKU 30(9),839-4511966)JAPAN CA-66-22616 V
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THE INTERPRETATION OF INITIAL RATE DATA WITH THE USE OF
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THE INTE _
HOUGEN-WATSON MODELS
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Ml CHE 62CMM MICHALKO E
CATALYTIC MIXING MANUFACTURE AND UTILIZATION
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MI CHE 660GC MICHALKO E
OXIDIZING C
US.3, 259,45-Mii.£j
CA-65-(P)-10413C
OXIDIZING GASEOUS COMBUSTIBLE WASTE PRODUCTS
US. 3, 259,454(CL23-2). JULY 5, 1966, APPL. 20,1962
MICHE 67MRL MICHALKO E
METHOD FOR REGENERATION OF LEAD CONTAMINATED CATALYSTS
GEN. 1.251.28KCL, B 01J ),OCT. 5. 1967,APPL. JAN. 11 ,1964
CA-68-rlP 1-61553 H
MICHJ 67KOS MICHALEK j VOSOLOBE j
KINETICS OF SULFUR-DIOXIDE OXIDATION ON AN INDUSTRIAL
VANADIUM CATALYST
CHEM. PRUM. 171101,527-3111967ICZECH CA-68-43558 J
MICIJ 66CR
MIKHK 67PSA MIKHAILOV K
MICIC J VUKOVIC D
CATALYTIC REACTORS
TEHNIKA IBELGRADE) 21.329-3311966) ( SERBOCROAT) CA-67-34236 E
LASTOCHKIN YV
SOKOLOVA AD
MISAY 67ASO
MITRP 65CGS
PREPARING SULFURIC-ACID BY THE NITROSE METHOD
USSR. 208,083 ICL.C.01BI,SEPT.14,1967,APPL.MAY 11,1964
CA-68-(P)-88647 D
MISAKA V YAMADA N
ABSORPTION OF SULFUR-01OX IDE BY CALCIUM-HYDROXIDE SLURRY
KAGAKU KOGAKU 311 9) , 925-6( 1967IJAPAN CA-68-32953 H
BHOMMIK TK KRISHNAMURTHY VA
MITRA p
BASU AN
THE CUMULATION OF GRANULAR SOLIDS IN A CATALYTIC REACTOR
INDIAN J. TECHNOL .3(61. 182-61 19651ENG CA-63-17498 D
MITS 67POG MITSUBISHI
PURIFICATION OF GASES BY SOLID ADSORPTION
FR.1,466,019ICL. B 010,A 61LI,JAN.13,1967 CA-67-(P)-57063 K
MI YAM 66APC MIYAJIMA M
AIR POLLUTION CONTROL MEASURES TAKEN AT THE POWER STATION
IN YOKKAICHI DISTRICT
NENRYO KYOKAISHI 451 474 I , 7 31-61 1966 I JAPAN CA-66-58665Z
MOCHI ft7LFE MOCHIDA I
YnNFDA Y
LINEAR FREE-ENERGY RELATIONSHIPS IN HETEROGENEOUS CATALYSIS
V. AN APPLICATION OF QUANTUM CHEMICAL REACTIVITY INDEXES
TO HETEROGENEOUS CATALYSIS
J.CATAL 9M I ,57-621 L9fe7)ENG CA-68-6730P
PONEG A3PFG MONEY G TATAPSK! A KIRCHEVA N
PURIFICATION OF FLUE-GASES FROM SULFUR-DIOXIDE
GODISHNIK NAUCHNOIZSLED. INST. KHIM. PROM. 2,5-20 (1963)
BULG CA-62-7407F
MONS 21CS MONSANTO CO.
CATALYST SUPPORTS
FR. 691,356 NOV.21, 1929
MONS 65CSM MONSANTO CO.
CATALYST SUPPORT MEANS
CA-2'5-(P)-1045 7
BRIT. 1,094,771 (CL.B 01J ) .DEC . 1 3, 1 967 US. APPL . JAN.2, 1964
AND JAN. 1,1965 CA-68-(P1-53837 P
MONS 65ROS MONSANTO CO.
REGENERATION OF SULFUR CONTAINING COMPOUNDS FROM BURNED
GASES
NETH.APPL.6,500,419 (CL .C . C IB I , JUL Y 16,196-5 CA-64-C PI -3097 G
MONT 65ASP MONTF.CATINI
A SIMPLIFIED PREPARATION FOR SULFURIC-ACID
ITAL. 688,338 ICL. C 018),MARCH 29,1965,APPL.FEB. 19,1963
CA-66-IP 1-87184 X
MONT 66CR MONTECATINI
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BRIT. 1,042.455 (CL. C 01B),SEPT.14,1966 CA-65-(P)-16547 B
MOORLP67GAL MOORE LP
GAS AND LIQUID CONTACT APPARATUS
U.S.3.322,411 (CL.261-96),MAY 30.1967,APPL. MARCH 29,1965
CA-67-(P1-55497 F
MORALES AM VILCHES AD
SPRAY COOLER TURFS IN SULFUR IC-AC ID MANUFACTURE
ION (MADRID) 26(2981,253-7(1966)SPAIN CA-65-14894
MDRAAM66SCT
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PREPARATION OF SULFURIC-ACID BY NITROSE METHOD
USSR 194,779 (CL. C OIBI,APRIL I 2,1967.APPL.MAR.2.1966
CA-68-61052 U
MORIJ A6AIC MORITZ J
APPARATUS FOR INTIMATE CONTACTING OF GAS WITH LIQUID
US. 3,278,170 (CL. 261-79),OCT. 11.1966.APPL. AUG.15.1963
CA-A6(P|-4?76 U
223
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MORIS 65ESG MOPIOKA S SAWAPA Y
EFFECT OF S02 GAS ON PITTING CORROSION
STAINLESS, STEEL
SHIORARA K
IF AUSTENTIC
MPSSRL66SAH
MOSSRL67SSP
ROSHOKU GIJUTSU 14( 12 I ,535-41 ( 1965 I JAPAN CA-64-19086 H
MOSS RL
THE STRUCTURE AND ACTIVITY OF HETEROGENEOUS CATALYSTS
CHEN.ENGR. ( LONDONINO. 199.CE 1 1 4-CE- 141 ( 1966 I ENG CA-65-6345 G
MOSS RL
"T*LVSTS EXAMINATION
PLATINM METALS REVIEW 1 11 4 I , 1 41-5( I 9671 ENG CA-68-72717 P
MOYEAJ65CRF MOVES AJ SMITH CR
COMPARATIVE RESULTS FOR THERMAL AND ELECTRONIC ACTIVATION OF
MIXTURES OF SULFUR -DIOXIDE AND OXYGEN
---------- '• -gDONIN0.19C,(1965IENG CA-63-1
-14413 F
CHEM.ENGR. (LONDON INO. 19C, I 196
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CATALYTIC REACTOR
CZECH.122, 715 ICL.B OUI,APRIL 1 5.1 9A7.APPL. JULY 13,196$
CA-68-1 P)-41455 Z
MUKHIP55TUO MUKHLENOV IP TRABER DG
THE USE OF A FLUIDIZED CATALYST FOR SULFUR-DIOXID
OXIDATION
KHIM.PROM. 1955,457-60 CA-50-6164 B
ES
MUKHIP57ACP
MUKHLENOV IP
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TRUDY LENNINGR""
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SARKITS VB DYBCHIKOVA Al
5HEMICAL PROCESS FOR THE PRODUCTION OF OXYGEN
DY LENNINGRAD. TEKHNOL. INST. IM.LENSOVETA 43,43-51(1957
MUKHIP59NCA MUKHLENOV IP TRABER or, MIKHALEV MF
NEW CONTACT APPARATUS FOR THE OXIDATION OF SULFUR-DIOXIDE IN
A FLUIDIZED CATALYST RED
MATERIALY MEZHVUZ .KONF .PO MASHINAM I APP.D IFFUZION. PROTESSOV
KAZANSK. KHIM.-TEKHNDL. INST.1959,52-63.CA-57-16128 A
MUKHIP63EDW MUKHLENOV IP IVANOVA RS SORRKO VE
EFFECT OF WATER VAPOR AND IRON COMPOUNDS ON THE ACTIVITY
OF VANADIUM CATALYSTS IN A FLUIDlZED-RED
ZH. PRIKL. KHIM. 36(4),730-6(19631 CA-59-3348 B
HUKHiP63Tun MUKHLENOV IP SARKITS VR OSIPOVA FN
THE USE OF CONTACT EQUIPMENT WITH A FLUIDIZED CATALYST BED
IN THE MANUFACTURING OF SULFUR IC-ACID
KHIM.PROM. 1963111),833-6. CA-6C-R920 C
MUKHIP64AMS MUKHLENOV IP TRARER DG DOBKINA El
A MECHANICALLY STABLE IRON CATALYST FOR THE OXIDATION OF
SULFUR-DIOXIDE
KHIM.PRHU. 19IS4I 4),24I-i
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MUKHIP6500C MUKHLENOV IP
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OXIDATION OF CONCENTRATED SULFUR-DIOXIDE
PROTOPOPOVA EA
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LAYER OF WEAR RESISTANT VANADIUM CATALYST
ZH.PRIKL.KHIM 38(BI,IA49'52(1965)RUSS CA-63-14366 H
MUKHIP6SPOV MUKHLENOV IP IVANOVA RS
POISONING OF VANADIUM CATALYSTS USED IN THE OXIDATION OF
SULFUR-DIOXIDE IN A FLUIDI ZED-BED
• — ~0),23Z8-f
ZH.PRIKL.KHIM. 38(10),
-30(1965IRUSS CA-64-1394 C
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SOME RESULTS OF A STUDY OF THE STRUCTURE OF A WEAR-RESISTANT
VANADIUM CATALYST
METODY ISSLED. KATAKLIZATOROV i KATALITICH. REAKTSII.SB
(NOVOSIBIRSK SIBIRK. OTD. AKAD. NAVK SSSR) 2.289-308
(1965IRUSS CA-65-9854 0
MUKHIP65TEO MUKHLENOV IP
DERYUZHKINA VI FILIPPOVA ZG
TRABER DG
THE EFFECT OF THE CONCENTRATIONS OF IMPREGNATING SOLUTIONS
UPON THE CHEMICAL COMPOSITION AND STRUCTURE OF A
MECHANICALLY STABLE VANADIUM CATALYST
KHIM PROM.41( 10). 751-411965IRUSS CA-64-9277 H
MUKHIP67SWR MUKHLENOV IP RUDENOK MI FILIPPOVA ZG
DOBKINA El DERYUZHKINA VI
STRUCTURE OF WEAR RESISTANT VANADIUM CATALYSTS FOR
SULFUR-rDIOXIOE OXIDATION IN A FLUI DI ZED-BED
KHIM.PROM. 43(6),432-6(1967IRUSS CA-6B-63031 K
MUKHV146IFC MUKHACHEV VM
INSTALLATION FOR CONTACT OXIDATION OF SULFUR-DIOXIDE GAS
USSR. 65.942 FEB 28,1946 CA-41-(PI-5268-A
NULABF67DMS H^g|KEYNg%ETAL s ON S|LfCEOUS CATALYST SUPPORTS FROM AMINE
COMPLEXES IN AQUEOUS AMMONIA SOLUTIONS
DEPOSITING METALS ON
COMPLEXES IN AQUEOUS AH _
U.S. 3,328.316 (CL. 252-455) .JUNE 27,1967 , APPL .MAY 4,1962
AND JAN. 24,1966 CA-67-( P )-76629 R
MULCMF67KRO MULCAHY MF STEVEN JR WARD JC
THE KINETICS OF REACTION BETWEEN OXYGEN ATOMS AND
S02 AN INVESTIGATION BY ELECTRON-SPIN-RESONANCE
J PHYS. CHEH^TK 71 , 21 24-31 (1 967»ENG CA-67-47603 X
MUSSGS66PCI MUSSER GS
A PERTURBATION CHROMATOGKAPHIC INVESTIGATION (IF
CHEMISORPTION AND CHEMICAL REACTION ON A SOLID CATALYST
UNIV. MICROFILMS (ANN ARBOR MICH.i,ORDER NO. 66-13,366.153
PP. DISS. ABSTR. B 27(41.1138-911966)ENG CA-fth-40988 X
NABIMN67CFF NABIEV MN KAMALOV KM DUBOVAYA VK
COMPOSITE FERTILIZER FROM PHOSPHATE NITRIC-ACID AMMONIA AND
SULFUR-DIOXIDE
UZR. KHIM. ZH. 1 l(l>,3-6( l"567)RUSS
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NACOM 67DSD NACOVSKY M
DETERMINATION OF SULFUR-DIOXIDE IN FLUE-GAS ON STREAM
COMBUSTION 381 71,35-81 1967 )ENG
NAGAS 66PIT NAGAURA S HURAKAWA S
PROBLEMS IN THE SURFACE CHEMISTRY OF METALS
SHINKU KAGAKU 14( 2-3) , 53-60( 19661 JAPAN CA-67-76488U
NAKAS 41COH NAKATA S MORITA N
CATALYTIC OXIDATION OF SULFUR-DIOXIDE BY HEAVY HYDROGEN
ON THE SURFACE OF A PLATINUM SPONGE
BULL. CHEM. SOC. JAPAN 16,463-71(19411 CA-41-4366 F IS.R.I
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CATALYTIC OXIDATION OF SULFUR-DIOXIDE WITH HEAVY OXYGEN
J. CHEM. SOC. JAPAN 62,519-24(19411 CA-35-7811
NAKAY 66CRC NAKANURA Y MORITA Z
THE CORROSION RATE OF CAST IRON BY SULFUR-01 OXIDE
-- ' -•• ~ 1-7(196" "
TECHMOL. REPT. KANSAI UNIV. 7,81-
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NAPIOH58COO NAPIER DH STONE MH
CATALYTIC OXIDATION OF SULFUR-DIOXIDE AT LOW CONCENTRATIONS
J.APPL.CHEM.8,781-611958) CA-53-7524.G
NATI 52ST NATIONAL SMELTING CO.LTD
SULFUR-TRIOXIDE
BRIT.672,311 MAY 21,1952 CA-46-(P)-10562 B
NECHN 35TIO NECHAEVA N
THE INFLUENCE OF SOME VARIABLES CHARACTERIZING THE QUENCHING
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J.PHYS.CHEM.(USSR )6, 76-821 19351 CA-29-7827-9
NEIPKV64POT NEIPERT KV MITIN EV
PRODUCTION OF TOWER SULFURIC-ACID BY A PROCEDURE INVOLVING
ACID CIRCULATION WITH A CROSS-OVER CYCLE
VESTN.TEKAN. I EKON.INFORM.NAUCHN.-ISSLED.INST.TEKHN.-EKON.
ISSLED.GOS.KOM.KHIM.PROM.PRI GOSPLANE SSSR(2 11964,18-20(RUSS
CA-62-4938 0
NEMKOG67AFC1 NEMKOVA OG
ELEMENT NI
ACTIVE FORM OF MANGANESE CATALYST IN THE OZONE CATALYTIC
METHOD OF OXIDATION OF SULFUR-DIOXIDE IN ACID SOLUTIONS
ZH.FIZ.KHIM. 39(9),2286-811967)
FREDRIKSON H
' ~URI
NESTIN67IWG NESTAAS IN
INDUSTRIAL WASTE-GAS PURIFICATION
TEK. UKEBL. 114( 12) , 226- 31 ( 19671 NORWEfi CA-67-46919 T
NEUMB 29TRM NEUMANN B
THE REACTION MECHANISM IN THE CONTACT SULfUK 1C-AC 10 PROCESS
AND THE METHOD OF ACTION OF ACTIVATORS
Z.FLECTROCHEM. 35, 42-51(1929) CA-23-1775
NEUMR 35DPO NEUMANN B SONNTAG A
DECOMPOSITION PRESSURES OF NITRATES AND SULFATES
MEASUREMENTS _
Z.ELECTROCHEM. 41,860-8(19351 CA-30-3306-2
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NITT 65VOA
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NEUMANN B
HEINTKE G
SULFURIC-ACID CATALYSIS WITH IRON-OXIDE
Z.ELEKTROCHEM. 43,246-54(1937) CA-31-4882-7
NEW ALL HE
AMMONIA PROCESS FOR REMOVAL OF SULFUR-DIOXIDE FROM FLUE
PROBLEMS AND CONTROL OF AIR POLLUTION 170-90 CA-50-5205 f
GAS
NIEDRACH LW
MCKEE OW
NOBLE METAL ALLOYS AS ANODE ELECTROCATALYSTS
PROC.ANNU.POWER SOURCES CONF.2I,6-10119671ENG CA-6B-76116 W
NIKOLAEV N SAFIN RS KARASEV AG
MASS TRANSFER AND ABSORPTION WITH REACTION IN ROTARY
• TYPE EQUIPMENT
TELPLO- 1 MASSOPERENOS 4, 84-92(19661RUSS CA-66-12486P
NITTO CHEMICAL INDUSTRY CO.LTD.
VANADIUM ON ALUMINA CATALYST FOR FLUIDIZED-BED OXIDATIONS
FR. 1,389, 673ICL B 01J) FEB. 19, 1965,CA-63-( P)-1 7206 8
NIXON WB UNIVERSAL OIL PRO
IMPROVING THE ACTIVITY OF
GFR. 1,146,036 (CL.B 01JI
CA-61-(P)-3734 B
ODUCTS
OXIDfC
,MAR.28,
CATALYSTS
1963,APPL.MAR.28,1961
NOVAK S
S02 UNDER PRESSURE
CHEM.PRUMYSL 13(101,516-21(1963) CA-60-4851 A
NURMATOV SM
RESISTANCE TO ACID
UZB. KHIM. ZH. ~
RAKHIMRAEV SM KANTSEPOL*SKI I IS
OF AUTOCLAVED CEMENTS
10(51,3-9{19661RUSS CA-66-40499 P
OHTAN
OKAO T530TS
NYROP JE
GASEOUS REACTIONS
DAN.54,-170,JAN.17,1938 CA-32-(PI-7H57-4
ODANAKA H
DETERMINATION OF THE STOICHIOMF.TR 1C NUMBER OF THE OXIDATION
OF SIILFUR-OIOX IDE
SHCKUBAI (TOKYO) 7( 2) , 160-fc( 1965 I JAPAN C A-6?-m96F
flHTA N
CATALYSTS FOR OXIDATION
KAGAKU TO SEIBUTSU 11 9) ,45P-7( 1 961!) JAPAN C A-6R-1 2^65 S
OKABA T
OXIDATION TREATMENT OF SULFUR-DIOXIDE
JAPAN,5415(53 I.OCT.21. CA-48-(Pl-l3183
227
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PAGF 67
OKAMT 60VCF
OKI Y 66TAC
OLECSM66PPA
OLSORM50COO
ONO S 63RAS
GRNEN 66EP
VANADIUM CATALYSTS FOR THE PRODUCTION OF SULFUR IC-ACID
JAPAN.7662< 19601,JUNE 22 CA-55-18033 H
OKI ¥
VAGI S
OSHIMA E
INDUE H
TEMPERATURE AND CONCENTRATION DISTRIBUTION IN A PACKED-BED
REACTOR
KOGAKU KOGAKU 30(41,341-8119661 JAPAN CA-64-17065 D
ss FQR PRODUCING AN ALUMINA CATALYST BASE
U.S. 3,249.557 ICL. 252-463),MAY 3.1966.APPL. JUNE 25.1962
CA-65-(PI-1824 D
OLSON RH SCHULER RW SMITH JM
CATALYTIC OXIDATION OF SULFUR-DIOXIDE EFFECT OF DIFFUSION
CHEM.ENG.PROGRESS 46, 614-24( 1950) CA-45-937H
ONO S
RADIATION EFFECTS ON SOLID CATALYSTS
NIPPON GENSHIRYOKU KENKYUSHO CHOSA HOKQKU NO.4024,14PP
(1963) JAPAN CA-64-18764 C
ORNE N
ELECTROSTATIC PRECIPITATOR
U.S. 3,284,990 ICL. 55-51.NOV.15,1966 APPL. NOV. 7.1963
CA-66-IP 1-39396 W
OSAMG 39TMO OSAME G
HIRAI T
THE MANUFACTURE OF SULFURIC-ACID BY MEANS OF VANADIUM
CATALYST ON AN INTERMEDIATE SCALE II. INCREASE OF THE
DRAFT RESISTANCE IN A SMALL CONVERTER
J.SDC.CHEM.IND.,JAPAN 42.SUPPL. 434(1939)CA-34-3025-8
OSAUG 43MOS OSAME G HIRAI T
MANUFACTURE OF SULFURIC-ACID BY VANADIUM CATALYST III
INCREASE OF THE DRAFT RESISTANCE IN THE LARGE CONVERTER
J.SOC.CHEM.IND.JAPAN 46,431-2119431
OS"66 APPL.JUNE 16.1964
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CATAL¥STS
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PAVLM 6QITV
PAYNJW64ROP PAYNE^JW
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CONTACT MULTIPLATE REACTOR FOR OXIDATION OF SULFUR-DIOXIDE
CZECH. 121.608CCL. C 01B) JAN.15,1967,APPL.MAY 13,1964
CA-6B-(PI-31444 F
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REJUVENATION OF PLATINUM CATALYST
U.S. 3,140.263 ICL. 252-412),JULY 7,1964,APPL.AUG.5,I960
PELZVE6TCLA PELZEL VE
CORROSION OF LEAD ALLOYS IN SULFUR I C-AC ID
METALL(BERLlN)21(8),B26-7( 1967)GER CF.CA-65 13353H
CA-67-93470 Z
PEREY»67UGS PERELYGIN YP AMMAS AY ROL*SHAKOV AP
USE OF GRAPHITE BLOCKS FOR PROTECTION OF SCRUBBING TOWERS
IN THE SULFURIC-ACIO PLANT OF UST-KAMENOGORSK LEAD-ZINC
TSVET. METAL. 40(51,44-5( 1967IRUSS CA-67-83484 T
PERRH 65»OR JJERR^H ^ REOUCING EMISSION OF OXIDES OF SULFUR FROM COAL
PRPC. AM. POWER CONF. 27,107-13( 1965IENG CA-64-15632 G
PETEA 6300S PETER A MATTHEWS F
OXIDATION OF SULFUR-DIOXIDE WITH NITROSE
NITROSYLSULFURIC ACID IN SULFURIC ACID
AND IN SIEVE PLATE COLUMNS
CHEM. TECH. I BERL 1N)1 51 I ?) , 720-31 1 963) CA-61-327 B
A SOLUTION OF
IN PACKED COLUMNS
PETEFH62RSA PETERSEN FH
REMOVAL OF SULFURIC-ACIO FCG FROM GASES
GER. 1,135,868 (CL. C 01BI,SEPT.6,1962,APPL.JULY 16,1960
CA-63-(Pl-2658 E
PETEG 594^ PETERSEN c
APPARATUS FOR CATALYTIC SULFUR-DIOXIDE OXIDATION
GER.1,054,431 JULY 2,1059 CA-55-IPI-10826 F
PETEG 59CDO PETERSEN G
CATALYTIC OXIDATION OF SULFUR-DIOXIDE
GER. 1,054,43!,APR.9, 1959 CA-55- ( P l-6flrn H
PETEH 66RSD PETERSEN H
REMOVAL OF SUl FlIR-OrOX IDE FROM INDUSTRIAL OASES,
NETH. APPL. 6,516,530 (CL C C IB I, JUNE 20,1966 GER. APPL.
DEC. 19,1964,AND APRIL 28,1965 2CPP. CA-66-(PI-4549Y
PETRNM47SOW PETROV NM
SULFUR OXIDATION WITH INTERNAL HEAT EXCHANGE
KHIM.PROM. 1947,NO.6, 166-71 CA-50-1M91 H
PETRNM66CFS PETROV NM
CONTROL FLOW-SHEETS IN THE OPERATION OF SULFUPIC-ACID
CONTACT INFORMATION
KHIM.PROM.42( 121,906-I2( I966IRUSS CA-66-477B3 K
PETRNM66HLT PETROV NM
HEAT LOSSES TO THE SURROUNDINGS AND PROCESS STABILITY OF A
CONTACT-TYPE H2S04 PLANT
KHIM.PROM. 42(51,44-811966IRUSS CA-65-16553F
PETRNM67CAF PETROV NM
CONTACT APPARATUS FOR OXIDIZING SULFUR-DIOXIDE
USSR. 190,873(CL.C 01BIJAN.14,1967,APPL.SEPT.7,1964
CA-68-IPI-23241 X
PICKWF66HOR PICKERING WF
HETEROGENEOUS OXIDATION REACTIONS
REV. PURE APPL. CHEM.(AUST.116(DEC.11B5-208(1966IENG
CA-66-98882 Z
PIERRJ66RPL PIERRE RJ SOLINHAE J
TERMINET R
RECOVERY PROCESS FOR LOW CONCENTRATIONS
MOLINET G
OF GASEOUS SULFUR
COMPOUNDS.CONTAINED.IN.RESIDUAL,GASES AND FUMES.
FR, 1,353,606 I CL
CA-61-IPI-27656
PIERCE RR
C 01 C
.FEB.28,1964,APPL. JAN.17,1963
ERC
, 2351-3( 1967IRUSS CA-68-31622 N
PINAVA67PGS PINAEV VA
PITELINA NP
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PURIFICATION OF GASES FROM SULFUR-DIOXIDE
U.S.S.R. 194,777 (CL. C 01BI,APRIL 12,1967,APPL. MARCH 29
1966 CA-68-IPI-61098 P
PISMLM66EOC PIS'MEN LM
EFFECT OF CONCENTRATION GRADIENTS OF REAGENTS AND THE
CATALYST PARTICLES
_ _TATE CONDITIONS
DOKL.AKAO.NAUK SSSR 67( 11 , 1 51-41 1966IRUSS CA-64-1503R C
TEMPERATURE ON THE EFFICIENCY OF POROUS
AND THE LIMITS OF EXISTENCE OF STEADY ~
PITENP6SRSO PITELINA NP PINAEV VA
REMOVING SULFUR-DIOXIDE FROM FLUE-GASES
U.S.S.R. 169,496 (CL. B 0101.MARCH 17,1965 APPL.
JULY 20,1963 CA-63-(BI-4010A
221
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PLATMS37CGT PLATONOV MS SPEVAKOVA KA
COLUMBIUM AND TANTALUM-OXIDES IN THE CONTACT PROCESS
J.APPLIED.CHEM.(USSR)10,1537-40(1937I(IN GERMAN 15401
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PLATMS3BCFO PLATONOV MS KRIVOSHLYKOV NF SPEVAKOVA KA
CATALYST FOR OXIDATION OF SULFUR-DIOXIDE AND OF ORGANIC
COMPOUNDS
RUSS.54,110,OCT.31,1933 CA-34-(PI-1588-6
PLUMAL68RSD
PLUME 54CSA
POLALS65HPI
POLLHA67SDF
POLTOM66ANA
PLUMLEY AL
SHUTKO FH
JONAKIN J
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REMOVAL OF SULFUR-DIOXIDE AND DUST FROM STACK GASES
PROC. AMER. POWER CONF. 29,592-614119671ENG.CA-68-89710 F
PLUMATE E
CATIONIC SCREENING AND SURFACE REACTION PHENOMENA
SILICATES IND. 19,97-107f19541 CA-48-8602 H
POLAK LS PSHEZHETSKII
HETEROGENEOUS PROCESSES IN RADIATION CATALYSIS
PURE APPL. CHEM. 1014 I,441-57(1965)ENG CA-67-7065 B
POLLOCK HA TOMANY JP FRIELING G
SULFUR-DIOXIDE AND FLY ASH REMOVAL FROM COAL BURNING
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AIR ENG. 9191,24-81 1967IENG. CA-67-111222 B
POLTORAK ON BORONIN VS
A NEW APPROACH TO THE STUDY OF ACTIVE CENTER OF CRYSTALLINE
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ZH. FIZ. KHIM, 40(111,2671-8711966IRUSS CA-66-41041 V
POLYM 34TMO POLYAKOV M '
THE MECHANISM OF SULFUR-DIOXIDE OXIDATION IN THE PRESENCE OF
VANADIUM CATALYSTS
BER. UKRAIN.HISS. FORSCH.-INST.PHYSIK.CHEM.3,149-51119341
CA-29-2668-7
POPECG67FSD
POPE CG
FLOW OF SULFUR-DIOXIDE OVER THE SURFACE OF SPHERON-612700)
GRAPHITIZED CARBON BLACK
TRANS. FARADAY SOC. 63(31,734-42119671ENG CA-66-10B561 K
POPON 6701R
POPOV 1C I N
ANGHEL P
POTOP P
DESIGNJJF AN INSTALLATION .FOR RETAINING
BRINOUS L
OF S02 <
FERTILIZI
RESIDUAL GASES IN A PLANT OF COMPLEX
ECONOMICALLY ADVANTAGEOUS CONDITIONS
REV. CHIH. (BUCHAREST) 18(1I,40-4(1967)(ROM) CA-66-115GC1F
POSTVF34TOO POSTN1KOV VF K1RULOV IP KUNIN Tl
THE OXIDATION OF GASES HIGH IN SULFUR-DIOXIDE AND OXYGEN IN
THE PRESENCE OF A VANADIUM CATALYST
J.APPL.CHEN.I USSR I 7,869-7111934) CA-29-2668-8
CONTA
SULFUR-DIOXIDE
KUNIN TI
POSTVF36CPO POSTNIKOV VF
ACT PROP
.__ _ D10XID-
J. APPL I ED CHEM. (U.S.S.R. 19, 1373-711936 1C A-31-2363-4
PROPERTIES OF'CHRnMiUM-OXIDE IN THE OXIDATION OF
AA
POTOP 66RSD POTOP P CREANGA L TEODORESCU C
RECOVERY OF SULFUR-DIOXIDE FROM RESIDUAL GASES BY WET
ABSORPTION IN TWO PURIFICATION STEPS
REV. CHIM. (BUCHAREST) 17(6),331-611966)(ROM.I CA-65-14896 E
KIRICHENKO NE
SOKOL'SKII AV
POZIME64POS POZIN ME MUKHLENOV IP
OGARKOV SP TARAT EY
PRODUCTION OF SULFUR IC-AC ID
USSR. 93, 398, JULY 22, 1964, APPL .JULY 13,1950 CA-6l-( PI-14225D
PRETST67PAP PRETORIUS ST MANDERSLOOT WGH
REMOVAL OF AIR POLLUTANTS FROM GASES BY REACTION WITH
PARTICULATE SOLIDS
POWDER TECHNOL. 1 ( 3) , 129-33( 1967)ENG CA-6A-71916 T
PROD 65POA
RAOEJ 67ARG
RAMAV 67CRK
RAMMVM65RAS
PPODUITS CHIMIOUES
PRODUCTION OF A GAS OF HIGH SULFUR-TRI OXIDE CONTENT
FR.1,395.732(CL.C 01RIAPRIL 16,1965 CA-63-(P)-l7527 H
RAOEMACHERS J HILL K MUELLER HO
ABRASION RESISTANT GRANULATED BOROPHOSPHATE
_ ._. ... 01B,tOEC.21,1967fAPPL.FEB.17,1965
AER. 1.256,635 (CL.
CA-68-MP 1-80066 T
RAMASWAMY V STERMOLE JF
CATALYST REGENERATION KINETICS
J. CHEM. ENG. DATA 12(41.552-4(1967IENG CA-68-33601 D
RAMM VM CHERTKOV 84 OORROMYSLOVA NS
RATE OF.ABSORPTION OF SOLUBLE GASES IN A WETTED WALL TUBE
ABSORPTION OF SO3 BY SULFURIC-ACID-MONOHYORATE
ZH. PRIKL. KHIM. 381 9),1980-711965IRUSS CA-64-3Z1 F
REBIPA64IMS REBINDER PA
INCREASING THE MECHANICAL STRENGTH OF POROUS DI
SHCHUKIN EO
MARGOLI!
REESRL RSD
RFINLU65SAS
LY
ADSORBENTS'ANO'CAfALYSTS
NAUCHN.OSNOVY POOBORA I PROIZV. KATALIZATPRDV.AKAO.NAUK SSSP
SIBIRSK.QTO. 1964.21-7(RUSSI CA-63-6352 H
REES RL
REMOVAL OF SULFUR-DIOXIDE FROM POWER PLANT STACK GASFS
BRITISH ELECTRICITY AUTHOR I TV,LONDON ENGLAND C4-50-5205F
REINLUFT
THE SIMULTANEOUS ABSORPTION OF
REOI
FLU
EDUCE
LUE-G
. 1.1
SULFUR-OXIDES AND ONE OR MORE
INDUSTRIAL GASES ESPECIALLY
CED SULFUR COMPOUNDS FROM
-GASES
GER. 1.193019 (CL. C CMRI.MAY 20, l«>65 , APPL . JUNE 2<*.l963
CA-63-P-39I7 F
223
231,
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REINLU66GAC REINLUFT
GAS-ABSORBING CHARCOALS
FR. 1.441,883 (CL. C 01BI, JUNE 10,1966 GER. APPL.
JULY 15,1964 CA-66-IR)-79951 E
RESHSM66RBC RESHETN1KOV SH
SOKOL'SKAYA AH
RELATION BETWEEN CATALYTIC ACTIVITY OF SOME METALS AND THEIR
SUBLIMATION HEATS
ZH.FIZ.KHIM. 40
EATS
(101,
2412-1511966IRUSS CA-66-32279 B
REUBBG60ANM REUBEN BG LINNETT JU BARBER M
A NEW METHOD OF EXAMINING THE REACTIONS OF OXYGEN ATOMS
SYMP. COMBUST.,8TH,PASADENA,CALIF.1960,97-102 CA-57-10570 C.
REUBF 67PIN
PROCED
. EOURES AND INSTALLATIONS FOR NEUTRALIZING TOXIC VAPORS
AND WASTE GASES
NASSER,LUFT BETR. 11(21.65-70(1967)GER. CA-66-98234 0
REZIIG65POM REZITSKII IG
PRODUCTION OF OLEUM IN THE MANUFACTURE OF SULFUR IC-ACID BY
THE SHORTENED CONTACT PROCESS
KHIM, PROM. 41(91 6811 1965IRUSS CA-64-12235 E
RHODRN67CDO RHODA RN VINES RF
CHEMICAL DEPOSITION OF CATALYTICALLY ACTIVE PLAT 1NUM ON
GRAPHITE AND METALLIC PONDERS AND SURFACES
BRIT. 1,097,010(CL. C 23C I ,DEC.29, 1 967 U.S.APPL.OCT.21 ,196$
CA-68-(P1-52649 S
RICHJT66AIT RICHARDSON JT TOUPS SS
APPARATUS FOR INDICATING THE THERMAL EMF AND AC
CONDUCTIVITY OF A CATALYST
U.S. 3, 2B3.243KL. 324-62),NOV. 1,1966, APPL. OCT.22.1962,3PP
CA-66-IP1-410878
RIDDES39CCF RIDOLER
S HEVGANDT AS
CONVERTER FOR OXIDIZING S02 TO S03
US. 2,195,738,APR 2 CA-34-(Pl-5255-6
FNRLEN HC
A'NEU METHOD FOR THE PREPARATION OF CONTACT CATALYSTS
RIOGO 49ANN RIDGE 0
A NEN M
CHEMISTRY AND INDUSTRY 1949,500 CA-43-8074 E
RIDLES29RPC RIDLER ES
REGENERATING PLATINUM CATALYSTS
U.S.2,006.221, JUNE 25 CA-29-rl PI-5610-9
RIDLES29RPQ RIDLER ES
REGENERATING PLATINUM CATALYSTS SUCH AS THOSE USED FOR
5 XIOAT ION OF SULFUR-DIOXIDE
1,980.829,NOV.13 CA-29-(P1-565-3
RIENG 59TWC RIENAECKER G
THEORY OF MIXED CATALYSTS
CHEM. TECH. (BERLIN I 11,246-50(1959)
RIENG 64CC RIENAECKER G
CARRIER CATALYSTS
SITZBER. DEUT. AKAD.NISS. BERLIN,KL CHEM.,GEOI.BIOL. 1964(3)
CA-61-7750 0
RIENG 64SAC RIENAECKER G SCHEVE E
SEMICONDUCTANCE AND CATALYSIS RELATION BETWEEN
CATALYTIC ACTIVITY STO ICHIOME TRI C COMPOSITION AND STATE
OF ELECTRON LINKAGE FOR N-CONDUCTING MIXED CATALYSTS OF
THE HOPCALITE-TYPE III. RELATION BETWEEN CATALYTIC
ACTIVITY STOICHIOMETRIC COMPOSITION AND RATE OF ELECTRON
LINKAGE FOR P-CONOUCTING MIXED CATALYSTS OF THE HOPCALITE
Z.ANORG.ALLGEM.CHEM.330(l-2l,27-33,34-9(l964)CA-61-6442 B
RIGHRA67EPO RIGHTMIRE RA FAY PS
ELECTROCHEMICAL PROCESS OF PRODUCING ELECTRICAL ENERGY BY
USING SULFUR-DIOXIDE FUEL AND HALOGEN OXIDANT
US. 3, 296.03HCL. 136-861 JAN. 3, 1967,APPL.OCT.29, 1965
CA-67-IP1-60361 M
RINCJB67CCW RINCKHOFF JB
CONTROLLING CORROSION IN WET-GAS SULFUR IC-AC10 PLANTS
CHEM ENG.(N.Y.174(241,158 1 60, 162( 1 9671 ENG CA-66-31416 V
RINCJB67MAI RINCKHT1FF JB
MAKING ACID IN IRON AND STEEL EQUIPMENT
CHEM. ENG. 74(18).160,162(1967IENG CA-67-101359 N
RINCJB67SAM RINCKHOFF JB
SULFURIC-ACID MANUFACTURE
US. 3.350,169 (CL.23-168),OCT.31,1967, CA-68-1PI-4523 Z
RITTLG63EUR RITTER LG
MALKIMAN VI
. ._ _. GLEIKHENGAUZ 1M
EFFECTIVENESS OF USING A RING-SHAPED CATALYST
VANADIEEVYE KATALIZATORY DLYA KONTAKTN. PROIZV.SEPNOI
KISLOTY.NAUCH.-ISSLEO.INST.UDORR. I INSEKTOFUNG..SB STATEI
1963,137-44 CA-60-2371 A
RITTLG6300F RITTER LG
UDINTSEVA VS SOROKINA NM
FOR THE ELEMENTS OF A_RING-SHAPEp_
OPTIMUM DIMENSIONS ..._ -__ ... - „
VANADIUM CATALYST AND THE SEARCH FOR NEN GRAIN SHAPES
VANADIFVYE KATALIZATORY OLVA KONTAKTN. PROIZV.SERNOI KISLOTV
NAUCHN-ISSLED.INST.UDDBOR. I INSEKTOFUNG.,SB.f
-36 CA-60-2369 G
.STATEI 1963,125
U.S
RIEKL 64AEA RIEKERT L
BAZZAN T
PIRO M
HETEROGEN
PROC.INTERN
CA-63-12361 G
ncra
EQUILIBRIUMS
EOUS CATALYT
. CONOR.CATA
MENZEL D STAIB M
AND REACTION SEQUENCES IN THE
. . 1C REACTIONS
TALYSIS,3RD,AMSTERDAM,1964 1,387-93 ENG
RIVOL 66CPS RIVC1LA L
ROMBARA G
CORROSION BEHAVIOR OF SOMF METALLIC MATERIALS IN LIQUID
SULFUR-DIOXIDE
INTERN. CDNGR. METAL. CORROSION,2ND,NEW YORK CITY 1961
413-23(Plin. 19h6IENC, CA-65-10280 f
236
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ROBf-r,W65EFF ROBERTS GW SATTERFIELO CN
EFFECTIVENESS FACTOR FOR POROUS CATALYSTS
HOOD KINETIC EXPRESSIONS
INO.ENG.CHEH.,FUNDAMENTAL 4(3).288,93119651ENG
ROBEGWA5F.FP ROBERTS GW SATTERFIELO CN
EFFECTIVENESS FACTORS FOR POROUS CATALYSTS
INO ENG. CHEM.,FUNDAMENTALS 4131,288-93(1965IENG
CA-63-6365 F
LANGMUIR-HINSHEL
RORSON S
SULFURIC-ACID
US. '
RORSS 25SA
ROBSS 28COO ROBSON S
RODEO 6BLAS
LAMBERT B
1,797,928 MARCH 24. CA-25-(P1-2817-7
CATALYTIC OXIDATION OF SULFUR-DIOXIDE
BRIT.320,930 JULY 25,1928 CA-(P)-2556-5
RHOEUALD D POMMRICH HJ NOUAK S
LABORATORY APPARATUS FOR STUDYING CATALYTIC PROCESSES IN
FLUIDIZED-BEDS
CHEM. TECH. (BERLIN) 201 21 , 111-1 3( 1 968)GER CA-68-88444 K
ROEGH 64MDP ROEGENER H
MEASUREMENT OF THE DEM-POINT OF FLUE-GASES AND ITS EFFECT
ON THE START OF CORROSION
MITT. VER. GROSSKESSELBESITZER NO. 93,381-6(19641GER.
ROGECE66RMB ROGERS CE MATTY RE RALSTON EL
REGENERATION OF MAGNESIUM-BISULFITE PULPING LIQUOR AND
ABSORPTION OF SULFUR-DIOXIDE DURING REGENERATION
U.S. 3.273.961 (CL.23-1311,SEPT. 26,1966,APPL. JULY 11,1958.
AND FEB. 12,1963 CA-66-P-4016U
ROGICZiiSOC ROGINSKII SZ
SELECTION OF CATALYSTS AND CONSTRUCTION OF CATALYTIC SYSTEMS
PROBL.KINETIKI I RATALIZA,AKAD.NAUK SSSR 11,15-35(1966)RUSS
ROGISZ670CM ROGINSKII SZ ALIEV RR 8ERMAN AD
LOKTEVA NK SEMENENKO El YANOVSKII MJ
DIFFERENTIAL CHROMATOGRAPH 1C METHOD OF STUDYING THE
KINETICS OF CATALYTIC REACTIONS
OOKL. AKAO. NAUK. SSSR 176(51.I114-16(19671RUSS CA-68-43570G
ROITVA58EOT ROITER VA KORNEICHUK GP STUKANOVSKAYA NA
RZAEV PB
EFFECT OF TRANSPORT ON THE KINETICS OF OXIDATION OF
SULFUR-DIOXIDE ON A BARIUM-ALUMINUM-VANADIUM CATALYST
INVESTIGATION BY THE DIAPHRAM METHOD
ZHUR.FIZ. KHIM 32, 2525-31(1958) CA-53-13753 A
ROITVA5BTRO ROITER VA STUKANOVSKAYA NA VOLIKOVSKAYA NS
THE ROLE OF THE OXYGEN OF VANA01UM-PENTOXIDE CATALYSTS (N
THE CATALYSIS OF OXIDATION
UKRAIN. KHIM.ZHUR.24,37-45(1958) CA-S2-15216 D
ROITVA60TKO
ROITVAfcOTMO
ROITVA62IKP
ROITER VA
VOLIKOVSKAYA N
THE KINETICS 0
CATALYST ~
STUKANOVSKAYA NA
GOLODETS GI
OXIDATION OF SULFUR-D
KORNEICHUK GP
XIDE ON A PLATINUM
UNDER EQUILIBRIUM CONDITIC _
KINETICA I KATALIZ 1,408-17(1960) CA-55-25433 E
ROITER VA
THE MECHANISM OF OXIDATION CATALYSIS BY METAL-OXIDES
KINETIKA I KATALIZ 1,NO. 1, 63-81 1960) CA-55-8003 I
ROITER VA
INVESTIGATION OF
IN THE STATE OF . _ . _
THE AID OF RADIOACTIVE S
RAOIOISOTOPES PHYS. SCI. INO..PROC. CONF. USE.COPENHAGEN
1960 3.435-4BIPUB. 1962) CA-57-15865 A
STUKANOV NA KORNEICHUK GP
THE KINETICS OF THE PROCESS(S02*.S02°S03I
P CHEMICAL EQUILIBRIUM ON A PT CATALYST BY
RniTVA65SOC ROITER VA GOLODETS GI
SIGNIFICANCE OF CHEMICAL FACTORS IN THE SELECTION OF
PROBL KINETIKI I KATALIZA AKAD.NAUK SSSR 11 , 56-65 (1965 IB USS
CA-65-14482 H
ROLLL 67RDF ROLL L
FROM FLUE-GASES
REMOVAL OF DUST . ,
GER. 1.243.153 (CL. B OlDl.JUNE 29,1967,APPL. DEC 23.1961
CA-67(P)r76122 V
ROSCSE66ELP ROSCHIN SE
EXPERIMENTAL LOCAL PURIFICATION OF HARMFUL ORGANIC AND
INORi
C DISCHARGES INTO THE ATMOSPHERE AND INTO BODIES
OF WATER
DOKL. NEFTEKHIM.SEKTS.BASHKIR.RESPUB. PRAVL. VSES.KHIM
OBSHCHEST. NO. 2, 103- 10( 1 966)RUSS CA-67-67378 F
ROSEEF46PPC ROSENBLATT EF POLLEN L
PLATINUM-PALLADIUM CATALYST FOR OXIDATION OF SULFUR-DIOXIDE
TO SULFUR-TRIOXIDE
U.S.2,418.851.APR.IS,1947. CA-41-1P)-4625E
ROSS 67MOA
ROSS 67TSO
ROTGH 26GOV
ROZnAY64A(lT
ROSSLER
MANUFACTURE OF AN OXIDATION CATALYSTS FOR USE AT HIGH
TEMPERATURES
FR. 1.467.334 ICL. B 01J.A 61LI JAN 27.1967 GER.APPL.FEB.3
AND SEPT.24,1965 CA-67-(P1-76123 W
ROSSLER
THE SEPARATION OF SUSPENDED NOBLE METAL CATALYSTS
BRIT. 1,096,260 (CL. B 010),DEC.20,1967 CA-68-(PI-727975
JER H STOEWENER F
GAS OR.VAPOR-PHASE CATALYTIC PROCESSES
ROTGER H
GAS OR.VA _ -_ ..
U.S. 1,828,380,OCT.20 CA-26-(P>-814-8
ROZOVSKII AY
ACTION OF THE REACTANT MIXTURE ON THE CATALYST IN THE COURSE
OF CATALYSIS
KINETIKA I KATALIZ S ( 4 ) , 609-1 M 1 964 )
237
238
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RUGHAL65POS R
RUGH AL
PRODUCTION OF SULFUR IC-AC ID
US. 3,172,725 (CL.Z3-168IMARCH 9,1965,APPL.JAN.25,1961
RUHR 62CRO RUHR-CHEMIE A.G.
CATALYTIC REMOVAL OF SULFUR COMPOUNDS FROM GASES
NETH.APPL. 299,076 (CL C 10K)AUG.10,1965 GER.APPL.OCT.10
1962 CA-64-(P)-6370 D
RUIZVP36TED RUIZOV VP KASHTANOV LI
THE EFFECT OF CATALVSTS AND ANTICATALVSTS ON THE KINETICS
RUMAES66POA
RYLULB60CC
RYLULB6000A
AND MECHANISM OF THE OXIDATION OF SULFUR-DIOXIDE
J.GEN.CHEM.(USSR 16, 732-471 1936) C A-30-701 9-5
RUMYA'NT'SEVA ES SOROKO VE MIKHALEV MF
MEGVINQV AA
PERFORMANCE OF AN INDUSTRIAL APPARATUS FOR THE OXIDATION OF
S02 IN A FLUIDIZED CATALYST BED
KH1M.PROM.42(6),448-50(1966>RUSS CA-65-15538 E
RYLUND LB TAMELE MM WILSON JN
CATALYSIS- OXIDATION, HYDRATION. DEHYDRATION AND CRACKING
CATALYSTS 7,1-9(1960) CA-54-14501 I
TAMELE
AMMONIA
MW
RYLUND LB
OXIDATION OF AMMONIA
AND SULFUR-DIOXIDE
CATALYSIS- OXIDATION.HYDRATION
CATALVSTS ~ ""
WILSON JN
AND METHANE CARBON-MONOXIDE
uxiuniluw.nTUKBiiun, DEHYDRATION AND CRACKING
7,281-345(1960! CA-54-14501 I
RZAEPB60KOT RZAEV PB ROITER VA KORNEICHUK
KINETICS OF .THE CATALYTIC FORMATION OF SULFURIC-ACID ON A
BAR lUHf-ALUMINUMrVANAOIUM CATALYSTS
UKRAIN. KHIM.ZHUR.26,161-7(1960) CA-54-21961 f
SADAE 67EOC SADA E WEN CY
EFFECT OF CATALYST POISONING ON THE OVERALL SELECTIVITY AND
SCI. 22(4).S59-71(1967)ENG CA-67-605a E
SAOOAS65COH SADOVSKII AS
CALCULATION OF HEAT TRANSFER COEFFICIENTS IN TUBULAR
VSES. KONF. KHIH. REAKTORAM 3,589-6C2|RUSS)CA-68-70566 S
I SAES 66PMR
I
S.A.E.S. GETTERS S.D.A.
POWDERED METAL REACTION
AGENTS PARTIALLY EMBEDDED IN "FTAL
GETTERS_S.
SUPPORTS
NETH.APPL.6,602,047 ICL.R 01J I .AUG. 18, 1966 I TAL. APPL.FEB.1 7
1965 CA-66-(P)-5362J
SALSF 52TCO SALSASrSERRA F
HF CATALYTIC OXIDATION OF SULFUR-DIOXIDE
CATALYST CHAMBER
CHIMIE AND INDUSTRIE 68 695-9C 1952)CA-47-5776 F
A STUDY OF THE
SALTVP60MCC SALTANOVA VP PIGUZOVA LI
HACROPOROUS CATALYST CARRIERS OF SILICA-GEL HR
ALUMINUM-SILICATE
USSR 127,243.MAR.25,I960 CA-54-(PI-18833 G
SALTVP63VCO SALTANOVA VP BELYAEVA TN
VANADIUH_CATALYSTS ON A RELAKS
OF SULFUR-DIOXIDE
VANADIEVYE KATALIZATORY DLYA KONTAKTN. PROI ZV. SERNOI KISLOTY
NAUCHN.-ISSLED.INST.UDnBR. ~ '"
-6 CA-60-2369 E
CARRIER FOR THE OXIDATION
u«i«RTN.PROIZV.SERNOI KIS
SEKTOFUNG.,SB.STATE! 1963,131
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MALAKHOV AI
SALTANOVA VP
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U.S.S.R. 170.915 (CL. B 01JI.MAY 11 ,1965,APPL. MARCH 13,1964
CA-63-(P)-14MOO
SAMOI 68DCT SAMOIL I
DATA CONCERNING THE BEHAVIOR OF THE VANADIUM CATALYSTS USED
IN ROMANIA
REV.CHIM.(BUCHAREST)18(7),405-111 1967IROMF. CA-68-63017 K
SANDJV64RBR
SANDO 63SCI
SANSJ 36DSC
SANDERS JV
RELATION BE
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J. AUSTF '
'ETWEEN REACTIVITY AND STRUCTURE OF METALLIC
KALIAN INST. METALS 9.63-70(1964) CA-61-8935 G
SANDALINAS 0 LOSTER R
S02 CONVERSION IN THE KACHKAROFF PROCESS
HRIT.CHEM.ENG.8, 618-2211963ICA-60-21B C
SANS J EHI. INGER A
DETERMINATION HF THE S»F.eD OF CONVERSION OF SULFUR-DIOXIDE
TO SULFUR-TRIOXIDE PN PASSING THROUGH A CATALYTIC LATTICE
BULL. SOC. CHIM.(193f.| CA-24-59412
SAROV 66SRF SAROCH V
SPHERICAL REACTOR FOR EXOTHERMIC CATALYTIC REACTION IN
GASEOUS PHASE
CZECH. 119, 915 (CL.B 01J) SEPT. 1 5. 1966, APPL SEPT. 25, 1964
CA-67-IPI-45412 K
SATAV 59TSO SATAVA V
THERMOGRAPH1C STUDY OF THE CATALYTIC OXIDATION OF
SULFUR -DIOXIDE ON VANADIUM-OXIDE
COLLECTION CZECHHSLOV. CHEM. COMMUNS. 24,3297-304(19591
CA-54-U672 D
A AF4 EOR
*F RADIOACTIVE COMPOUNDS PN CATALYTIC OXIDATION OF
-DIOXIDE
NnVOCHERKASKHGO IND. INST. IM. S. ORDZHONI KIDfF 6
SAVEW 52TLO
SULFUR-niOXIDE
IZVEST. NDVrjCHERKASKDGO IND_
SER.KHIM.45-641 19401 CA-35-1583-8
THE LAW'OF MASS-ACTION AS THE BASIS FOR CALCULATING THE BEST
YIELD FROM TECHNICAL AND ECONOMIC STANDPOINTS
CHEM.7TG. 76.37-4H IPS?) CA-46-69rn R
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SAVIEI66EOS
SCHCED65SPP
SCHEC 64RIW
SCHEJ 64EAO
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5AVINKOVA El OLESOVA AL
EFFECT OF SULFURIC-ACID CONCENTRATION ON REGENERATION OF
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KHIM.TEKHNOL.MINER.UDOBR.(TASHKENT
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MICAL THEORY OF THE
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KINETIKA I KATALIZ 6(4 I , 641-5O(1965 IRUSS CA-63-15B71
REMOVING IK .
DECHEMA .MONOGRAPH 52(895-9111.229-4011964)GER. CA-62-10099F
INORGANIC WASTES IN THE CHEMICAL INDUSTRY
SCHEVE J
EFFECT OF ADDITIVES ON OXIDE CATALYSTS
S5fH3
SENICONDUCTIVITV
ILLUSTRATED'SY INVESTIGATIONS USING~MIXED OXlSITckTALYSTS
Z.ANORG.ALLGEM. CHEM. 333( 1-3) . 143-53( 1964IGER CA-62-111B7 C
SCHMAHL NG
HETEROGENEOUS GAS CATALYSIS AT HIGH TEMPERATURES
Z.PHYSIK.CHEM.(F.RANKFURTI42(l-2>,13-31(1964) CA-61-12681 A
SCHNEIDER P . . HITSCHKA P
EFFECT OF INTERNAL DIFFUSION ON
IRREVERSIBL
MOLES
COLLECTION CZECH
.. ._ _.. CATALYTIC REACTIONS I
REACTION WITHOUT A CHANGE IN THE NUMBER OF
CHEM.COMMUN. 30,146-57(19651CA-62-9843 A
SCHNP 66EID SCHNEIDER P MITSCHKA P
EFFECT .OF INTERNAL DIFFUSION ON CATALYTIC REACTIONS
EFFECT OF PARTICLE SHAPE ON REACTION WITH LANGNUIR
HINSHELUOOD TYPE OF KINETICS
COLLECTION CZECH. CHEM. COMMUN. 31{31,1205-13(19661ENG
CA-64-1834736
SCHOR 67ACE SCHOBER R
APPARATUS FOR CATALYTIC EXOTHERMIC REACTIONS IN THE GAS
GER.l,254,604(CL R 01JI,NOV.23,1967,APPL.OCT.29,196*
CA-6B-IRI-70538J
SCHRF 32TOO SCHREIBER F
THE OXIDATION OF SULFUROUS-ACID
METALLBORSE 22,209-10,241-2, 273-4, 305-6,369-70 .401-2,434-5
METALLBORSE 227209-1
(19321 CA-26-3076-2
SCHRR 64EOI
SCHRADER R
EFFECT OF IONI
SCHOENHERR.S
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BY ACTION OF X-RAY RADIATION
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OXIDATION OF
_ .ULFUR-DIOXIDE-OXYGEN
SULFUROUS-ACID TO SULFURIC-ACID
SYSTEM II TH
BY ACTION OF
Z.ANORG.ALLGEM CHEM 33K5-6i,289-97(i964i CA-6i-i2833 c
SCHH 52COT SCHWARZ-BERGKAMPH
CALCULATION OF THE SULFUR-TRIOXIDE CATALYSIS
MITT.CHEM. FORSCH.-INST. HIRTSCH. OSTERR.6,50-2C19521
CA-46-9811 F
SCHWEF66ROA SCHWARZENBEK EF
REGENERATION OF A PLATINUM CATALYST BY OXIDATION AND
TREATMENT WITH A HYDROGEN-CONTAINING GAS
U.S.3,230,179 (CL.252-416),JAN.18.1966 CA-64-(P)-8977 C
SCHMGM63EMC
SCHMGM64EMC
SCHWGM67IMC
SCHWAB GM KALDIS E
THE ELECTRONIC MECHANISM OF THE CATALYTIC FORMATION OF S03
NATURWISSENSCAFTEN 50(151,516-17(1963) CA-59-8161 A
SCHWAB GM KALOIS E
ELECTRONIC MECHANISM OF THE CATALYTIC S03 FORMATION ON CR203
CONTACTS
Z.PHYSIK. CHEM.(FRANFURT) 42(1-21.72-81(19641 CA-64-12681 B
SCHWAB GM DERLETH H
INVERS MIXED CATALYSTS SULFUR-TRIOXIDE SYNTHESIS USING
-ATALYST ON A SILVER CARRIER
Z.PHYS.CHEM.(FRANKFURT AM MAINJ 53( 1-61 Vl-B( 1967 )GER
CA-66-108700 E
SCHUGM67MSC
SCHHR 29TEO SCHWARZ R
THE EFFEC
Z.ANORG A
SCHYF 61 DOT SCHVTIL F
SCHWAB GM
METHODS OF STUDYING CATALYSIS
CHEM.-ING.-TECH. 39(20),1191-711967IGER CA-68-33614 K
KUNZER W
THE EFFECT OF ELECTRICAL-DISCHARGE UPON CHEMICAL REACTIONS
Z.ANORG ALLGEM CHEM 183,376-83(1929) CA-24-790-1
SCHWALB H
DEPENDENCE OF THE CATALYTIC OXIDATION OF
THE PARTICLE SIZE OF THE CATALYST IN AC
FIXED-BEDS
CHEN. ENG. SCI.
SULFUR-DIOXIDE ON
14.367-7411961IGERM
ATED AND
CA-55-19373 A
SCOTWD67FSW SCOTT WO HOBBS PV
THE FORMATION OF SULFATE IN WATER DROPLETS
J. ATMOS. SCI. 24(11, 54-7(1967)ENG. CA-66-108894W
SEFEB 67SAP SEFEROVIC B
SULFURIC-ACIO PRODUCTION PROCESSING TECHNIQUE DEVELOPMENT
TEHNIKA(BELGRADEI22(2).319-23(1967ICROAT CA-68-61021 H
SEGAAV60CWG SEGAL AY
CLEANING WASTE GASES IN THE DOROGOWILOVSK CHEMICAL PLANT
VESTN. TEKHN. I EKOU. INFORM. NAUCHN.- ISSLEO. COS. KOM.
KHIM. I NEFT. PROM. PR I COS PLANE SSSR 1963(91. 30-1.
CA-61-1420F
SEIYT 61TCO SEIYAMA T
SUENAGA A
THERXOOYNAMIC CONSIDERATION ON THE I
CARBON-MONOXIDE AND SULFUR-DIOX ID!
SAKAI W
:ATALYTIC OXIDATION OF
NIPPON KAGAKU ZASSHI 82.292-8(1961) CA-55-19422 E
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KAGAWA
SEIYT 66HS of;TEcrOR FOR GASEOUS COMPONENTS WITH SEMICONDUCTIVE THIN
SELO 27CPO
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SELIM 67RC
SHABA°63SUF
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17 CA-23-(PI-940-3
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POROUS SUPPORT FOR FLUIDIZFD-BED CATALYSTS
GEP. 1,249,828
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SHV4CL63CMF SHVARTS GL MARKAROVA LS
CONSTRUCTION MATERIALS FOR FILTERING APPARATUS IN
NICKEL COBALT PRODUCTION
TP..VSES.NAUCH.-ISSUED.KC1NSTR. INST.KHIH.MASHINOSTR. NO.45
35-42I1963IRUSS CA-67-35438J
SlOnYS67CBC SIOQRKINA YS DAL'NIKOVICH RF
CORROSION BEHAVIOR OF CHROMIUM-NICKEL-MOLVBDENUM-COPPER
STEELS IN SULFURIC AND EXTRACTION PHOSPHORIC-ACIDS
KHM. NEFT. MASHINOSTR. 1967(51,25-6(RUSS)
SIEOJ 64MCC ^fSjfU^NisH OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE INFLUENCE OF TEMPERATURE AND TIME OF CARBON
8ESORPT10N ON ADSORPTION AND OXIDATION OF H2S AND S02
ZIKI CHEM. 38(7/81,11Sl-60(1964 I POL CA-62-8425 C
SIEDJ 64RSG SIEOLEHSKI J
REMOVAL OF S02 FROM GASES BY USING VARIOUS GRADES OF
ACTIVATED CARBON
BRZEMVSL CHEM. 43(41,203-711964) CA-61-2758 C
SIEOJ 650NA SIEDLEWSKI J
DETERMINATION OF THE NUMBER OF ACTIVE CENTERS ON THE CARBON
SURFACE BY THE ELECTROCHEMICAL METHOD IN OXYGEN
CHEMISORPTION
RCCZNIKI CHEM. 39(3),425-3511965)POL
1 ° MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
THE CONTRIBUTION OF CARBON FREE-RADICALS IN THE
S02 TO S03 OXIDATION PROCESS
RCCZNIKI CHEM. 39(2 1,263-7211965)POL CA-63-3662 H
SIEDJ 66HCQ SIEDLEMSKI J TRAWINSKI S
MECHANISM OF CATALYTIC OXIDATION ON ACTIVATED CARBON
CORRELATION BETWEEN THE CONCENTRATION OF FREE-RADICALS OF
CARBON AND ITS CATALYTIC ACTIVITY IN H2S AND S02 OXIDATION
PROCESSES
"CCZNIKI CHEM. 40(6).n83-90(1966)POL.
SI EM 65SAC SIEMENS-SCHUCKERTWERKE A.G.
SEPARATING A CONSTITUENT FROM A GAS STREAM
BRIT. 1,003,419 (CL. B 04B,C).SEPT.2.1965,GER.APPL.MAY 20,61
CA-43-(P)-14405G
SILI 33C SILICA GEL CORP
CATALYSTS
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SIMEA 66COT
CO
MECEK A KADLEC B
MPUTATION OF THE ADIABATIC
OF SULFUR-DIOXIDE
CHEM.PRUMYSL 16(41,201-311966ICZECH
TEMPERATURE FOR THE
CA-65-5067 A
MICHALEK J
OXIDATION
SINFJH67CSM SINFELT JH
CATALYSIS OVER SUPPORTED METALS
CHEM. ENG.PROGR. SYMP. SER. 63(73),i6-25(i967)ENG
CA-67-67964 U
SIROGD48DIS SIROTKIN GO
DETERIORATION IN SERVICE OF VANADIUM CATALYSTS USED FOR
OXIDATION OF SULFUR-DIOXIDE
ZHUR.PRIKLAD.KHIM(J.APPL.CHEM) 21,245-8(1948) CA-43-2744 E
SLINMG61TCQ SLIN'KO HG
_ BESKOV VS
THE COMPUTATION OF CONTACT APPARATUS FOR THE OXIDATION OF
SULFUR-DIOXIDE ON AN ADIABATIC CATALYST LAYER
KHIM.PROM. 1961, 826-31 CA-57-5581 D
SILVAJ67SMQ SILVESTRI AJ
ESTRI AJ ZAHNER JC
ALGEBRAIC MANIPULATIONS OF THF RATE EQUATIONS OF CERTAIN
CATALYTIC REACTIONS WITH A OIGITAL COMPUTER
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SLINHG640SS ._ _
OPTIMUM SHAPE AND SIZE OF CATALYST GRAINS
NAUCHN. OSNOVY POOBORA I PROIZV.KATALIZATOROV,AKAD.NAUK SSSR
SIBIRSK. OT0.1964,68-74(RUSS) CA-63-4985 F
SMITRI68APP SMITH Rl . .
AIR-POLLUTION PROBLEMS OF THE PHOSPHATE INDUSTRY
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CA—68—81180N
SMYSNI67CCT SMYSLOV NI FAINSHTEIN GI SHKLVAR BV
SKORICHENKO AV KAVNATSKAYA RS
COMBINATION CONTACT-TOWER PROCESS FOR SULFURIC-ACID
KHI1.PROM. 43( 81,586-921 1967IRUSS CA-67-11 8644. L
SOC. 27SA SOC. GENERALE METALLURGIOUE DE HOBOKEN
SULFURIC-ACIO
BRIT. 286,980,AUG.23.1927 CA-23-(P1-486-6
SOCI C-5POC SOCIETE DES FORGES
PURIFICATION OF COMBUSTION GASES
FR. 1,399,747 (CL.C 01BI.MAY 21,
SOCI 66CS SOCIETE GENERALE OE PRODUITS REFRACTORIES
FR.1,440,817 (CL. B 01J) JUNE 3.1966.APPL. APRIL 22, 1965
CA-66-1 P 1-41089 S
SOCIET56000 SOCIETE ANPN. OES MANUFACTURE DES GLACES ET PRODUI TS
DETERMINATIPNJIF THE OEGREEJJf OXIDATION OF SULFUR-DIOXIDE
IN THE MANUFACTURE OF SULFUR IC-AC ID
DE SAINT-GOBAIN.CHAUNY C CIREY. RRI T.
CA-51-(P)-9105 H
759, 056, OCT. 10,1956
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S.n.G.n.E.
PRHCESS AND APPARATUS
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. Sf'KQLSKAYA AM
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OCPENDENCE OF CATALYTIC ACTIVITY OF METAL ON THEIR POSITION
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r./\-A7-;>6079 R
SOLT-Ut4FCC SOLOV'EV RI KUNIN TI
RFTECT OF CARRIERS ON THE ACTIVITIES AND PROPERTIES OF
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NAUCHN. OSNnVY PODBORO I PROIZV. KATAL I ZATOROV t AKAO. NAUK
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PEOUCTION OF AMBIENT Am CONCENTRATION OF SULFUR-OXIDES
"lESF.NT AND FUTURE PRHSPECTS
U.S.iPUHLIC HEALTH SERV. PUBL . NO. 1649, 1 61 -9( 19661 ENG
rA-6S-158Pl 0
SPE1GLFR G
SULFUR-OXIDES IN FLUF.-GAS AND IN THE ATMOSDHERE A PROBLEM OF
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OuSSELDORF VD1-VERLAG.1965
CA-64-10308 C
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SPERHA^TCO SPERANSKII BA
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HeTEROGENFOllS RADIATION CATALYSIS
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HfTEPHGFNEIiJS RADIATION CATALYSIS AND RADIOACTIVE CATALYSIS
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SOUIAM67APT SCUIRFS AM
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UTION THE CONTROL OF SULFUR-DIOXIDE FROM POWER
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STACKl" " THE REMOVAL OF SIH.H1H-DI OXIDE FROM STACK GASES
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STADPM65DIT STADNIK PM
DIFFERENCE IN THE OXIDATION PROCESS
STETSnVICH KG
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AND HYDROGEN ON A PLATINUM CATALYST UNDER THE CONDITIONS
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OF CHILLING AND THE APPLICATION OF AN ELECTRIC FIELD
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1965.94-10KRUSS) CA-6«-«318 G
STADVP64KOS STADNIK VP KORNEICHUK GP ROITER VA
KINETICS OF SULFUR-DIOXIDE OXIDATION ON VANAOIUM-PENTOXIDE
UK.KHIM.ZH. 30(91,919-25119641RUSS CA-62-5930 F
STADVP64MOT STADNIK VP
STAN 64CRF
_ . KORNEICHUK GP
METHODS OF TESTING THE ACTIVITY OF CATALYSTS
UKR.KHIM.ZH 30(3),252-61 1964ICA-61-70G
ATALYST REGENERATION FOR THE CONVERSION OF HYDROCARBONS
~ - ~ - , AUG. 20, 1964 US. APPL. JULY 7,1960
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STEGER JF ARNOTT RJ SIEGAL LA
VANADIUM-OXIDES AS OXIDATION CATALYSTS
IND. CHEM. *7, 1424-30(19551 CA-49-15415 B
STELLING PO EKLUND RBM
APPARATUS FOR CHEMICAL REACTIONS
BRIT. 669,311 APR. 2,1952 CA-46-1PI-9902 B
STELLING PO
ACCELERATIONS OF CHEMICAL REACTIONS BY VIBRATION
EKLUND RBM
SWEN.138,857;jAN.27,1953~ CA-47-TPI-4714-G
STERMOLE JF RAMASWAMY V
CATALYST REGENERATION KINETICS
J.CHEM.ENG.DAT A. 12(4), 552-41 1967IENG
STETTER G
CATALYST
BRIT. 720.025.DEC. 15,1954 CA-49-IPJ-7155 E
STETSOVICH KG
OXIDATION OF SULFUR-DIOXIDE OVER A PLATINUM CATALYST UNDER
THE CONDITIONS OF ANNEALING AND THE APPLICATION OF AN
-. __ CATALYST
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ELECTRIC CHARGE TO THE CATALYST
NAUK.ZAP.UZHGORODS'K.DERZH.UNIV.
STOPK 65EOS STOPPERKA K
ELECTROSTATIC DEPOSITION OF SULFUR IC-ACI0 MISTS FROM THE
WASTE GASES OF SULFURIC-ACID MANUFACTURE
STAUB 25(11),508-121 1965)GER CA-64-12702 C
STORDH64SZO STORMONT DH
SYNTHETIC ZEOLITES OFFER UNIQUE PROPERTIES AS CATALYST
SUPPORTS
OIL GAS J. 62(471,50-3(19641 CA-62-4656 C
21*8
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S1TMRA66ESP
STREZV64CCA
STOWE RA HAVER RP
EFFICIENT SCREENING OF PROCESS VARIABLES
IND. ENG. CHEM. 58( 2 I , 36-40( 1966) ENG CA-64-13791 F
STREL'NIKOVA ZV LEBEDEV VP
COMPARATIVE CATALYTIC ACTIVITY OF CENTERS ON THE SUB
CRYSTALS AND OF AN INERT CARRIER
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NEW METHOD FOR DETERMINING THE COMPOSITION OF THE ACTIVE
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STUPEV4900S STUPOCHENKO EV
OXIDATION OF SULFUR-DIOXIDE CAUSED BY IMPACTS OF SLOW
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SUGAH 65ESD SUGAMARA H SHI MOD A IRA 5
EFFECT OF SULFUR-DIOXIDE ON THE ATMOSPHERIC CORROSION OF
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NIPPON KINZOKU GAKKAISHI 29(121,1210-15(19651 JAPAN
CA-67-7S690 S
SUGAS 65RBA SUGA S
THE RELATION BETWEEN ACCELERATED CORROSION TESTS AND
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THE RELATION BETWEEN ACCELERATED CORROSION TESTS AND OUTDOOR
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SUGIK 66RCC SUGIYANA K TAKAHASHI T
REACTION OF CALCIUM-CHLORIDE WITH SULFUR-TRIDXIDE
KOGYO KAGAKU ZASSHI 691 41 , 605-71 1966) JAPAN CA-66-98929 V
SURNLN64EOO SURNEV LN BLIZNAKOV G
EFFECT OF OXYGEN AND SULFUR-DIOXIDE ON SOME ELFCTRIC
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EFFECT OF GAS ENVIRONMENT ON CERTAIN SEMICONDUCTOR
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NEFTEPERABOTKA I NEFTEKHIM..NAUCHN. TEKHN. SB. 1964(6),16-17
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SWINA 66VCU SWINARSKI A LASIEHICZ K JERZY K
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PARLAGH G
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CATALYTIC PROPERTIES OF FERRIC-HYDROXIDE IN THE OXIDATION OF
SULFUR-DIOXIDE BY ATMOSPHERIC OXYGEN
J.PHYS.CHEM.(U.S.S.R.) 9,421-30(19371 CA-31-6830-9
TANAK 66GRO TANAKA K TAMARU K
GENERAL RULE OF THE CATALYTIC ACTIVITY OF METALS
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TARTR 66EDP TARTARELLI R CAPOVANI M MORELLI F
EFFECTS OF THE DISTRIBUTION OF PORE LENGTHS IN CATALYST
PARTICLES ON THE CATALYST EFFICIENCY IN AN IRREVERSIBLE
SURFACE REACTION OF THE FIRST ORDER
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TARTR 66PSC TARTARELLI R
PORE STRUCTURE IN CATALYSTS
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TARTR 67SSF TARTARELLI R MORELLI F
SELECTIVITY FOR SUCCESSIVE FIRST ORDER REACTION AND CATALYST
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1957 CA-61-(P)-75D
TELLAJ68ROS TELLER AJ
RECOVERY OF SULFUR-OXIDES FROM STACK GASES
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TFRMMA66APC TERMEULEN MA
AIO POLLUTION CONTROL BY OIL REFINERIES
INT. CLEAN AIR CONGR..PROC..PROC..LONDON 1966(PT.I I,92-5 ENG
CA—68—62448 Q
TEPMR 64NCF TFPMINF.L R
NEW CATALYST FOR THE RECOVERY OF
AND THEIR TRANSFORMATIONS INTO SULFUR-TR IOXIOE
FR.l,357,675.(CL. B OIJ.C 10K I APR. 10,1964, FEB. 11 ,1963
CA-61-IPI-11376 C
TERNAI62NAP TERNOVSKAYA Al
A NEW ABSORPTION PROCESS
KHIM. PROM. 1962(7),5GI-6IRUSS). CA-63-7921H
TETEVI67CWY TETERYUKDV VI FEOKTISTOV GI NUSINOV YE
COMPRESSORS WITH HYDRAULIC PISTONS FOR CORROSIVE GASES
PROM. ENERG, 22( 4) , 47-9( 1967IRIISS .
THIEEW67EGS THIELE F.W
THE EFFECT OF GRAIN SIZE ON CATALYST PERFORMANCE
AUCR.SCI. 55(2),176-a4U167)ENr, CA-68- 72705 K
TIKHAV40TMO TIKHHNOV AV
THF MECHANISM OF CATALYSIS AND A METHOD FOR THE SELECTION
OF CATALYSTS FROM THF PfMNT OF VIEW OF INTFRMEOIATF
P-JOO'JCTS
TRUDY.VSESOYUZ. PROM. AKAD.194C.NO.2,I4-2T KHIM REFFRAT.ZHUR
4.M0.1* 11(1941 I CA-38-910-9
TILHB 6ftRCM TII.HAIID »
PFMOVAL (IF CARttON-MONOXlOE AND SULFUR-ACIOS FPOM FLUE-GASES
FP. 1.45Z.OBB (f.L.F 23 J I , SEPT. 9, 1 966, APPL .JUNE 16.19ft?
TINKJD64EFI TINKLER JD METZNER AB
EFFECTIVENESS FACTOR IN NONISOTHFPMAL CATALYST PELIE1S
CHFM.ENG SCI 19( 7 1, 50 M 196«) C«-61-fl9?6 (•
TIPPCF64EOV TI"PFR CFH WILLIAMS BH
EFFECT OF VANADIUM PENTOXIDE ON GAS-PHASh COMPUSTION I THE
CARBON-MONOXIDE SULRJR-DIOXIDF OXYGEN SYSTEM
J.APPLIED. CHEM I LONDON)14,315-2411 964) CA-6I-H9406 B
TIPPJW67MIS TIPPING JH
METHODS OF INVESTIGATING THE SURFACE PROPERTIES OF CATALYSTS
LEICESTER CHFM. Rfv. NO.H,42-911967IFNG CA-67-366«8 F
TITAT 4fiCOS 1ITANI T NAKATA S
CATALYTIC OXIDATION OF SIJLFUR-OI OXIDE RY HEAVY HYDROGEN
ON A PLATINUM SPONGE
PROP.. IMP. ACAI). (TOKYIj) 1^,184-6(10401 CA-34-7169
2E1
252
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1ITAT 52HHA TITANI T
HEAVY HYDROGEN AND OXYGEN
ANN. REPT. ST. I. WORKS FAC. SCI. OSAKA UNI V. 1 ,39-5111952 )
CA-4B-4275 E
TODEOM660RO TODES OH
OVERALL RATE
OF CATALYTIC RE ACT IONSAS INFLUENCED BY THF
INHOMOGENEITY OF THE FLUIDI/EO BED
OOKL. AKAO NAUK SSSR 1 71 ( 2 I, 410-1 3(1966)RUSS CA-66-79991 T
66TEO TOOO N
THE EFFECTS OF RADIATION ON CATALYSTS
KAGAKU TU KOGYO
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PAGE 93
VAMOC 6.?snn VANDAOF r
Sn«»F OHSHP VAT IONS ON THE CALCULATION OF HETEROGENEOUS
CATALYSIS
INO.r.HIM. (PARIS) 49,415-27(1962)FR. CA-61-15395 G
VAUL-4L35AFC VARLAMOV «L
APPARATUS FOR OX I DI/. ING SULFUP-D I OX IDE
BUSS. 44, 020, NOV. 30, 1935 CA-32- ( P 1-3105
\M»L-'«L54GdS VAPLAMHV
OF SULFIJR-DlflXIDE UN FLUIDIZEO VANADIUM CATALYSTS
AO. XinE IN THE REDUCTION
IFUROUS GAS BY CARRnN-MONPXIIU
ANAIS ASSOC OUIM. BRASIL 4,155-62(19451 CA-41-256 F
VYAKDA67GCC VYAKHIREV OA GAVRILINA IY
GAS-CHROMATOGKAPHY IN CATALYSIS RESEARCH
USP. KHIM. 36(2),362-75( 1967IRUSS CA-A6-988R4 R
255
256
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PAGF 95
WAKAN 66SOS
WALTJH40SA
WAY DF66HAA
WEI J 66HTI
WEILJA29CSF
WENGP 18SOT
WERTH 64TBD
WERTH 65TBD
WESTNG67STP
WEYCS 55TRO
SELECTIVITY OF SUCCESS IV£HREACTIONS IN CYLINDRICAL CATALYSTS
KAGAKU KOGAKU 30« B) , 745-81 1966> JAPAN CA-66-2259 P
WALTHALL JH
SULFURIC-ACIO
U.S.2,188,324 JAN.30
METHOD AND APPARATUS FOR A FLUID I ZED-BED REACTION
U.S. 3,242.195(CL.260-346.4) HAR.22t1966tAPPL.FEB.6,1963
CA-64-(PI-19016-H
WEI J
MAXIMUM TEMPERATURE INSIDE A POROUS CATALYST
CHEH.ENG.SCI. 21( 12 ) 11171-831 1966IENG CA-66-108678 D
WEIL JA
CATALYSTS SUITABU
BRIT. 334,286, JUN
FOR.gXIDIZING SULFUR-DIOXIDE TO TRIOXIOE
-(P)-1045-5
WENGER P
STUDY OF TH!
GAS IN THI
ANN.CHIM. M
1,1929
URTER C
OXIDATION OF SULFURDUS-ANHYDRIDE AND AMMONIA
i PRESENCE OF PLATINUM AND RHODIUM
IAL 23,97-104(1910) CA-121864-1
UERTH H
THE BAYER DOUBLE-CONTACT PROCESS FOR CONVERTING S02 TO S03
DECHENA MONOGRAPH 521895-911»,219-2711964IGER.CA-62-10104 F
.B*Yt» DUAL_CATALVST_PRgCESS,
WERTH H.
CHEM"lNGR:=fECH~37(2T,99-I6Ul965) CA-62-12778 C
WESTON NG
SULFUR-TRIOXIDE PROCESSING
CHEM. PROCESS ENG. 4B(3),61-41 1967) ENG CA-66-96976 J
THEJJIOLE.OF yANApVL-SULFATE IN THE PROCESS OF CATALYTIC
?fI,3,329-32(19551 CA-50-3939 C
OXIDATION OF SULFUR-DIOX IDI
BULL,ACAD.POLON.SCI.CLASSE "
WEYCS 65AOP WEVCHERT S KOLAKOWSKA H
ACTIVITY OF PURE VANADIUM-PENTOXIDE IN CONTACT OXIDATION OF
S02
CHEM. STOSOWANA.SER.A 913 I,273-85(1965)POL CA-64-2784 G
WEYCS 65DOT WEVCHERT S KUBINSKI I URBANE* A
DETERMINATION OF THE ACTUAL RATE OF OXIDATION OF
SULFUR-DIOXIDE
PREMYSL CHEM. 45(1),15-19(19S6)POL
CA-65-5067 B
WEYCS 66ios WEYCHERT s KOLAKOWSKA H
INFLUENCE OF SORPTION ON THE ACTIVITY OF PURE .V205 IN THE
CHEMl0STOSOWANA*slR.A 10(1 I.3-101I96MPOL CA-65-1436 H
WHEAJB68RFP WHEATCROFT JB WILLACY
REMOVING FINE PARTICLES FRO
IAR
M GASES
U.S. 3,363,398 (CL.55-51.JAN. 16,1968,APPL.MARCH 23,1965
CA-68-(P)-81189 X
WHIGW 67ROV
WICKE 5IMAH
WICKK 57CRI
WHIGHAM W
RECOVERY OF VANADIUM FROM PETROLFUM
CAN. 770,058 (CL.75-1C2) OCT.24,1967
CA-6B-IPI-42089 V
WICKE E
MASS AND HEAT TRANSFER IN GAS-SOLID SYSTEM
CHIMIA(SHITZ)5,173-8l(1951 I CA-46-3333 E
WICKERT K
CHEMICAL REACTIONS IN THE COMBUSTION SPACE OF SLAGGING
BOILERS
BRFNNSTOFF-WARME-KRAFT 9,105-18(19571 CA-51-9122 H
WICKK 61COO WICKERT K
CATALYTIC OXIDATION OF SULFUR-DIOXIDE AS A FUNCTION OF
RESIDENCE TIME OF THE GASES IN THE REACTION CHAMBER
BRENNSTOFF-WAERME-KPAFT 14.NO.1,20-1(1962) CA-56-12355 A
WICKK 65TCB WICKFRT K
TYPES OF CORROSION AND BEHAVIOR OF METALS AND ADDITIVES IN
BOILER FURNACES
WERKSTOFFE KORROSION 16112),1C48-54(1965IGER CA-64-7772 E
WICKK 67STP WICKERT K
SULFUR-TRIOXIDE DETERMINATION IN DUST-LADEN AND OUST-FREE
COMBUSTION GASES
ERCOEL KOHLE 20( 8) , 56H-72I 1967IGER. CA-6B-84117H
WINTHA59ALO WINTERMUTE HA
WOJCBW68TTC
WOLFF 62GCM
AQUEOUS LIQUIDS OF HIGH OXIDIZING POTENTIAL
US. 2,867,573 JAN.6,1959 CA-53-(PI-5927 G
WOJCIECHOWSKI BW
A THEORETICAL TREATMENT OF CATALYST DECAY
CAN. J. CHEM. ENG. 46(1 I,48-52(1968>ENG CA-6B-72711 J
WOLF F LORENZ F
GAS-CHROMATQGRAPHIC METHODS FOR TESTING CATALYSTS
ABHANU.. DEUT. AKAD. WISS. BERLIN,KL. CHEM. .GEOL.HIOL. 1962
II),507-11 CA-59-4581 E
WOLKT 66ETC WOLKENSTEIN T
WRONC 63ELC
WUNDG 64SAR
ELECTRONIC THEORY OF CATALYSIS
IND. CHIM. BELGE 311 8) , 755-6711 966(FR CA-66-41032 T
WRONKOWSKI C
ECONOMIC LOSSES CAUSED BY EXPELLING S02 TO THF ATMOSPHERE
GAZ.WODA TECH.SANIT. 37(21,60-1(1963) CA-62-135S A
WUNDERLICH G WEBER H
SULFURIC-ACIO RECOVERY FROM COKE OVEN OFF-GAS
GF.R. I, 170.911 (CL. C 01RIMAY 27, 1964, APPL . APR.24,1963
CA-61-80960
257
258
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YAKIEM34TEO VAKIHETS EM BAKINA NP
THE EFFECT OF CARBON-MONOXIDE AND CARBON-DIOXIDE ON THE
COURSE OF THE CONTACT OXIDATION OF SULFUR-DIOXIDE TO
SULFUR-TRIOXIDE
J.CHEM.IND.IMOSKOWI1934,N0.2,21-3 CA-28-3844-5
VAMAH 67CR
VAMAMOTO H INAASA N
CATALYTIC REACTOR
BRIT. 1,089,353 (CL. B 01J) NOV.1.1967,APPL.AUG.27,1965
OKI I. I,\jeit3?3 II
CA-6B-(P 1-60845 T
YANEJF65PAS VANES JF FERNANDEZ CI SANTOS AM
POLYMER ABSORBENT FOR SULFUR-DIOXIDE THAT PROMOTES ITS
OXIDATION
SPAN. 309,492. JAN.1,196S,APPL.JULY 28,1964 CA-63-1955 F
YASHEV65GHF
YASHKE EV
OSMyL'KEVICH VA
AMELIN AG
PETRONSKII VA
GLASS-WOOL FILTERS FOR TRAPPING SULFURIC-flXIDE MIST
KHIN PROM. 1965I3I.196-200IRUSS) CA-63-1499 F
YONEY 67LFE VONEDA Y
LINEAR FREE-ENERGY RELAT _
IV. REGIONAL ANALYSIS FOR SOLID ACID CAT
J.CATAL. 9(11.51-61 1967IENG CA-68-6729V
NSHIPS IN HETEROGENi
ALY!
OUS CATALYSIS
YUZKSL34HCU YU
Z'KO SL
HETEROGENEOUS CATALYSIS USING A TUBE CATALYST I. NATURE OF
THE METHOD
UKRAIN.KHIM.ZHUR.25, 260-71 19591 CA-53-18337 0
ZAKHMS58KSO ZAKHAR"EVSK11 MS
CHANG MC
ON
KINETIC STUDIES OF THE OXIDATION OF SULFUR-DIOXIDE
VANADIUM CATALYSTS PROMOTED BY ALKALI METAL SALTS
TUNG PEI JEN NIN TA HSUCH-TZU JAN K'O HSUCH PAD l.NO.6,117
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SOKOL'SKII DV
PROPERTiES'bF Pf AND PD
ZAKUG066EOS ZAKUMBAEVA CD
EFFECTS OF SURFACE ACTIVE
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TR.INSf.KHIM.NAUK,AKAD.NAUK.KAZ.SSR.14,9-56(19661RUSS
ZALON 3300S ZALOGIN N
ZALOGIN N NECHAEVA N
OXIDATION OF SULFUR-DIOXIDE IN A HIGH-FREQUENCY DISCHARGE
J.PHYS.CHEM.I USSR 14,832-44 (19331 CA-29-1330-516
ZALON 35POT ZALOGIN N
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THE INFLUENCE OF LONG WAVES OF A
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BILITY OF ..
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REACTIONS
ZAMYFF63SGC ZAMVATINA FF
STRONG, GRANULATED CATALYST FOR THF OXIDATION OF
SULFUR-DIOXIDE IN A SUSPENDED LAYER OF CATALYST
VANAOIEVVE KATALIZATORV DLVA KONTAKTN.PROIZV.SERNOI KISLOTV
NAUCHN.-ISSLED. INST. UD08R. I INSEKTOFUNG..SB.STATEI 1963
145-9 CA-60-2368 F
ZAWAEA65ROS ZAWADZKI EA
REMOVAL OF SULFUR-DIOXIDE FROM FLUE-GASES
GAS PHASE OXIDATION PROCESS
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CA-65-2892 B
THE BCR CATALYTIC
ZELETI66QAO ZFLENVAK T
OUALITATIV
CESSE
I ANALYSIS OFKEQUA
' CATALYTIC_PRPCESS_IN_A
• I
SLI.N'KO MG
KINEf.KAfAL. 71 5)7865-7311966fRUSSCA-66-14364 M
IONS DESCRIBING EXOTHERMIC
- -- - POROUS PLATE
ZEMSIF65CRS ZEMSKOV IF
CONTINUOUS REMOVAL OF SULF
BY A FLUIDIZED LAYER OF
R-DIOXIDE FROM GAS MIXTURES
FLUIDIZED LAYER OF SOLID GRANULAR ABSORBENT
SSHIKH UCHEBN. ZAVEOENNII,KHIM. I KHIM. TEKHNOL.
-B(1965)RUSS CA-63-2645H
0( 11,94-
ZHORYM67KRS ZHOROV YM PANCHENKOV GM LAZ'YAN VI
KINETICS OF REGENERATION OF SPHERICAL CATALYST IMMOBILE
ZH^*FIZ. KHIM.41(71,1574-9(1967)RUSS CA-67-l?0382 F
ZILBDE68RDI ZIL'BERMAN DE
REDUCING DISCHARGE INTO THE ATMOSPHERE OF SULFUR IC-AC ID MIST
MINIMIZING SULFURIC-ACID VAPOR DISCHARGE INTO THE
ATMOSPH6RE
KHIM.PROM. 44( ll,60( 196BIRUSS CA-68-81165 M
ZIMINA65ROC ZIMINA NA FRIDSHTEIN IL
REGENERATION OF CATALYSTS
U.S.S.R. 177,413 (CL. B 01 J ) ,OFC . 1 8, 1965 , APPL. JUNES ,1967
CA-64-(PI-16700 D
ZLATSG66PCC ZLATKIN SG SEMKINA NV STRELOV KK
.YAKOVA NP KACHKINA ZU
EPARATIQN OF CORyNOyM_CARRIERS FOR.CATALYSTS
>, APPL.
RELYAKOVA NP KACHKINA ZU
PREPARATION OF CORUNDUM CARRIERS . .... .
U.S.S.R. 184,260 (CL.B 01JI,JULV 21 ,1966,APPL.FEB.25.1965
CA-66-(PI-14*31 R
NOVRUZOV AA
ZULFZG66SAI ZUL'FUGAROV 7G ZUL'FUGAROVA LS
DZHAFAROVA EM
A STUDY OF ADSORPTION ISOTHERMS ON OXIDE FORMS OF
METALSILICATE CARRIERS AND CATALYSTS
VETSI AKAD. NAVUR RELARUSK. SSR,SER.KHIN.NAVUK 1966(21.14-19
RUSS. CA-65-14421 E
2EO
259
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BIBLIOGRAPHIC DATA *•*»?? "«; , ,
SHEET APTD-0677
4. Title tod SOMiflo
Applicability of Catalytic Oxldati.
meat of Hew Processes for Removing
Volume III - Indexed Bibliography
ft 3. Recipient'* Aeceioioo No.
5. Kepon Dote
>n to the Develop- August 1970
7. AnfaoKi) 8. E. OpterKUCll (Project Leader) «• Pcrforainf Orsuiuiioo Repi.
S. M. Hehta, A. H. Konstam. D. L. Zanders. B.-R.Stroi "*'
9. Perfomuu OQuiKuoo Hu> ud Addten
Monsanto 'Research Corporation-. -
Dayton Laboratory
Dayton. Ohio 45407
IZ Spoo>ofio> 0>fioiMiaa Hone ud Addte» • • •
Environmental Health Service, U. S
5710 Booster Pike
Cincinnati, Ohio 45277
10. Projeci/T>ik/Votk Unit No.
11. Coou.ct/Gi.nt No.
PH 22-68-12
IX Type ol RepoR * Period
I Co»«ed
nlstratlon
Dept. of HEW
14.
IS. SupoJemeoutr Nowe
It. Abomcio
This report presents an Indexed bibliography which provides access to
all information accumulated during the literature search phase of this
project. During the first phase, a search was made of all literature
for pertinent information relating to the catalytic oxidation of sulfur
dioxide. •_ L—,
17. Eer Vodo oad Docaaea Ao»ly»i«. I/O. Deicfipion
Indexes (documentation)
' Catalysis
Catalytic converters
Oxidation
Sulfur dioxide
176. Uenifien/Opoo-E*ded Teau
Catalytic oxidation
I7& COSATI FieldAImp 1 3/ B
IS. AraJllfcUilT Tm I
Unlimited
FOMM HTI»>n flO. Ml .
Flue gases
Rlectric power plants
IV.. Secuiliy dm (Thli 2k Tib. of P>l»
Rnecwiiy (•!••• (ibU u nice
uKOMo'ae «out>>i«Ti si^
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DISCLAIMER
This report was furnished to the Air
Pollution Control Office by Monsanto Research 'Corporation
Dayton Laboratory
Dayton, Ohio 45407
In fulfillment of Contract Ho. PH 22-68-12
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