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Chemical_Process_Equipment.pdf

Title

: Chemical Process Equipment Selection and Design

Subject

:

Author

: Stanley M. Walas

Keywords : Referex

Page: 585

is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page: 586

catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids

4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included

combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page: 587

13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and

are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page: 588

for hydrodealkylatisn and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page: 595

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(3)

File

:

B568F9B71AFF6F12BB1B9F5694CE1.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 10

and hydrogenation and dehydrogenation reactions. Hydrogen Blistering. Hydrogen blistering is caused by atomic hydrogen

(4)

File

:

Air_Pollution_Prevention_Control_Handbook.pdf

Title

: Handbook of Air Pollution Prevention and Control

Subject

:

Author

: Nicholas P. Cheremisinoff

Keywords : Referex

Page: 110

processes: (1) dehydrogenation of naphthenes to aromatics; (2) dehydrocyclization of paraffins to

4) hydrocracking. The dehydrogenation reactions are very endothermic, requiring that the hydrocarbon stream be

Page: 116

and propylene, catalytic dehydrogenation of isobutane, and conversion of tertiary butyl alcohol recovered as

Page: 571

85, 88 catalytic dehydrogenation of isobutane, 99 catalytic hydrocracking, 85, 90 catalytic reforming, 85,

Page: 572

of paraffins, 93 dehydrogenation reactions, 93 dehydrogenation of naphthenes, 93 density, 160 deoxyribonucleic acid

dehydrogenation reactions, 93 dehydrogenation of naphthenes, 93 density, 160 deoxyribonucleic acid (DNA), 13

(5)

File

:

Modeling_of_Chemical_Kinetics_and_Reactor_Design.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 412

homogeneous, vapor-phase dehydrogenation of benzene in a tubular-flow reactor considered two reactions:

Page: 418

F for the dehydrogenation of benzene using the Runge-Kutta fourth order method

Page: 419

of reactions for dehydrogenation of benzene. Rates of reaction (lb mol/ft3 •

Page: 549

125) Examples: decomposition, dehydrogenation, and sublimation reactions If k1 and k2 denote the forward

(6)

File

:

Pollution_Prevention_Through_Process_Integration.pdf

Title

: 92188.pdf

Subject

:

Author

:

Keywords : Referex

Page: 167

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File

:

Intro_to_ChemE_Analysis_Using_MATHEMATICA.pdf

Title

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Subject

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Author

:

Keywords : Referex

Page: 374

The hydrogenation and dehydrogenation of alkenes and alkanes are reversible processes that favor the

Page: 511

For example, the dehydrogenation of saturated alkanes and alkyl aromatics to produce alkenes and

that is, the dehydrogenation of alkanes to alkenes and hydrogen, continuous removal of either

(8)

File

:

Applied_Process_Design_VOLUME1_3E.pdf

Title

: APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL

PLANTS, Volume 1, 3rd Edition

Subject

:

Author

: Ernest E. Ludwig

Keywords : Referex

Page: 543

(9)

File

:

Chemistry_of_Petrochemical_Processes_2E.pdf

Title

:

Subject

:

Author

:

Keywords : Referex

Page: 4

of Propane, 172, Dehydrogenation of Propane 172, Nitration of Propane 173 n-Butane Chemicals

Page: 44

developed for the dehydrogenation of propane to propylene for petrochemical use. Propylene has always

Page: 45

for olefin production. Dehydrogenation of n-butane to butenes and to butadiene is an (Chapter 3). Dehydrogenation of isobutane produces isobutene, which is a reactant for the

Page: 46

production except the dehydrogenation of propane. Catalyst CH3CH2–CH3 r CH3CH=CH2+H2Table

Page: 47

for ethylene production. Dehydrogenation of butanes is a second source of butenes. However, this

Page: 50

are the catalytic dehydrogenation of butanes and butenes, and dehydration of 1,4-butanediol. Butadiene

isoprene is the dehydrogenation of C5 olefins (tertiary amylenes) obtained by the extraction

Page: 74

such as the dehydrogenation of naphthenes and the dehydrocyclization of paraffins to aromatics. Catalytic

Page: 75

catalytic sites, hydrogenation-dehydrogenation sites and acid sites. The former sites are provided by

best known hydrogenation-dehydrogenation catalyst and the latter (acid sites) promote carbonium ion

(10)

aromatics are the dehydrogenation of naphthenes and the dehydrocyclization of paraffins. The first reaction

represented by the dehydrogenation of cyclohexane to benzene. This reaction is fast; it reaches

lower than the dehydrogenation of cyclohexanes. Table 3-6 shows the effect of temperature

Page: 78

to aromatics (dehydrogenation of naphthenes and dehydrocyclization of paraffins) produce hydrogen and are

Page: 81

important because the dehydrogenation of naphthenes to aromatics can reach equilibrium faster than the

paraffins. Because the dehydrogenation of naphthenes and the dehydrocyclization of paraffins are highly endothermic,

Page: 92

sites and hydrogenation-dehydrogenation sites. Amorphous silica-alumina, zeolites, or a mixture of them

30 The hydrogenation-dehydrogenation activity, on the other hand, is provided by catalysts such

Page: 93

catalyst with hydrogenation-dehydrogenation activity, the olefins are hydrogenated to paraffinic compounds. This reaction

Page: 101

formation and hydrogenation-dehydrogenation reactions. The reaction may start by forming a carbocation via

Page: 104

a free radical dehydrogenation reaction, where hydrogen is a coproduct: CH3CH3 r CH2=CH2

Page: 105

tube alloys catalyze dehydrogenation and formation of coke. Coke formation reduces product yields, increases

Page: 116

by the catalytic dehydrogenation of butanes or a butane/butene mixture. CH3CH2CH2CH3 r CH2=

first step involves dehydrogenation of the butanes to a mixture of butenes which are Lummus fixed-bed dehydrogenation of C4 mixture to butadiene.52 The process may also used for the dehydrogenation of mixed amylenes to isoprene. In the process, the hot

(11)

Page: 117

uses an oxidative-dehydrogenation catalyst in the presence of air and steam. The C4 Hydrogen released from dehydrogenation reacts with oxygen, thus removing it from the equilibrium mixture

of the oxidative dehydrogenation process was made by Welch et al. They concluded that

Page: 118

comes from the dehydrogenation of C5 olefin fractions from cracking processes, several schemes are

for isoprene production. Dehydrogenation of Tertiary Amylenes (Shell Process) t-Amylenes

(2-aqueous sulfuric acid. Dehydrogenation of t-amylenes over a dehydrogenation catalyst produces isoprene. The

amylenes over a dehydrogenation catalyst produces isoprene. The overall conversion and recovery of

t-Page: 142

olefin by a dehydrogenation step: The carbide mechanism, however, does not explain the formation

Page: 185

as a fumigant. DEHYDROGENATION OF PROPANE (Propene Production) The catalytic dehydrogenation of propane

Production) The catalytic dehydrogenation of propane is a selective reaction that produces mainly propene:

Lummus-Crest Catofin dehydrogenation process.3 For a given dehydrogenation system, i.e., operating

For a given dehydrogenation system, i.e., operating temperature and pressure, thermodynamic theory provides

Page: 186

Lummus Crest Catofin dehydrogenation process:3 (1) reactor, (2) compressor, (3)

temperature on the dehydrogenation of different light paraffins.4 NITRATION OF PROPANE (Production

Page: 187

temperature on the dehydrogenation of light paraffins at one atmosphere.4 Nitropropane reacts with

Page: 191

to be the dehydrogenation of propane and butane to the corresponding olefins followed by the predominance of dehydrogenation and cracking. Methane and ethane are by-products from the

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Page: 193

hydrogen (from dehydrogenation of propane) through the reverse water gas shift reaction. CO2

Page: 194

isomerization followed by dehydrogenation to isobutene. The Catofin process is currently used to dehydrogenate

Page: 211

activated copper-catalyzed dehydrogenation of ethanol. Currently, acetaldehyde is obtained from ethylene by using

oxidation or the dehydrogenation of ethanol (approximately 500°C for the oxidation and C for the dehydrogenation). Ethylene oxidation is carried out through oxidation-reduction (redox).

Page: 219

are produced by dehydrogenation of nparaffins, dehydrochlorination of monochloroparaffins, or by oligomerization of ethylene

complexes catalyze the dehydrogenation of n-paraffins to α-olefins. The reaction uses a

Page: 242

isopropanol by a dehydrogenation, oxidation, or a combined oxidation dehydrogenation route. The dehydrogenation reaction

a combined oxidation dehydrogenation route. The dehydrogenation reaction is carried out using either copper

dehydrogenation route. The dehydrogenation reaction is carried out using either copper or zinc oxide

Page: 243

used for the dehydrogenation reaction. Acetone can also be coproduced with allyl alcohol in produced from the dehydrogenation of isopropanol and adsorbed on the catalyst surface selectively hydrogenates

Page: 255

by the catalyzed dehydrogenation of sec-butanol over zinc oxide or brass at about

Page: 258

produce MEK by dehydrogenation, as mentioned earlier. 2-Butanol is also used as a

Page: 269

remainder comes from dehydrogenation of n-butane or n-butene streams (Chapter 3).

(13)

11 billion pounds. Dehydrogenation of ethylbenzene to styrene occurs over a wide variety of used for the dehydrogenation reaction. Typical reaction

Page: 280

followed by catalytic dehydrogenation to styrene:8 Figure 10-3. Schematic diagram of the

Page: 283

α-methylstyrene by dehydrogenation. α-Methylstyrene is used as a monomer for polymer manufacture

Page: 288

corresponding n-paraffins. Dehydrogenation of nparaffins to monoolefins using a newly developed dehydrogenation catalyst

a newly developed dehydrogenation catalyst by UOP has been reviewed by Vora et al. monoolefins. Because the dehydrogenation product contains a higher concentration of olefins for a given

9) combines the dehydrogenation of n-paraffins and the alkylation of benzene.17 Monoolefins

Monoolefins from the dehydrogenation section are introduced to a fixed-bed alkylation reactor over

Page: 289

(1) pacol dehydrogenation reactor, (2) gas-liquid separation, (3) reactor for

Page: 295

to benzene. The dehydrogenation of cyclohexane Figure 10-12. Effect of hydrogen purity and

Page: 297

over a hydrogenation-dehydrogenation catalyst such as nickel. The hydrodealkylation is essentially a hydrocracking

Page: 393

from, 259 from dehydrogenation of C4, 103–104 polymerization with Li compounds, 308 polymers

62–65 Catofin dehydrogenation process, 173 Cellulose, 301 Chain addition polymerization, 304–308 Charactenzation

Page: 394

from, 315 Cycloparaffins dehydrogenation of, 63 in crude oils, 13 DDT, 278 DEA ( to butadiene, 104 Dehydrogenation of ter-amylenes, 105 butanes and butenes, 103 cycloparaffins, 63

(14)

process for C4 dehydrogenation, 103 Malathion, 243 Maleic anhydride 1,4-butanediol from, 242–243

Page: 400

scheme, 297 Lummus dehydrogenation process for butadiene, 103 Physical absorption, 3 Physical adsorption, 3,

Page: 401

173 cracking, 97 dehydrogenation, 172 Lummus-Crest process, 173 temperature effect on, 172 heating

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File

:

Adhesion_Science_and_Engineering_VOLUME2.pdf

Title

: Surfaces, Chemistry & Applications

Subject

:

Author

: M. Chaudhury and A.V. Pocius

Keywords : Referex

Page: 614

through hydrogenation and dehydrogenation reactions. Hydrogenation of the first conjugated carbon-carbon double bond

Page: 624

catalyst, followed by dehydrogenation; a-methylstyrene is obtained as a byproduct in the production

(16)

File

:

Coulson_Richardsons_Chemical_Engineering_Volume_2.pdf

Title

:

Subject

:

Author

:

Keywords : Referex

Page: 568

(17)

File

:

Fluid_Catalytic_Cracking_Handbook_2E.pdf

Title

: 92155.pdf

Subject

:

Author

:

Keywords :

Page: 77

reactions, such as dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation

dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation means polymerization,

Page: 78

matrix. Nickel promotes dehydrogenation reactions, removing hydrogen from stable compounds and making unstable olefins,

Page: 79

activity to promote dehydrogenation reactions, A small amount of nickel in the FCC feed to increase the dehydrogenation reactions. Chlorides in the feed reactivate aged nickel, resulting in

an indicator of dehydrogenation reactions. However, the ratio is sensitive to the reactor temperature

Page: 80

Vanadium also promotes dehydrogenation reactions, but less than nickel. Vanadium"s contribution to hydrogen yield

Page: 119

indicative of the dehydrogenation activity of the metals on the catalyst. The addition of

Page: 123

catalyst. They cause dehydrogenation reactions, which increase hydrogen production and decrease gasoline yields. Vanadium

Page: 137

with nickel, the dehydrogenation reactions that are

Page: 141

7. 8. Naphthenes Dehydrogenation Dealkylation Condensation C7H14 - n-C8H18 lso-C3H Ar-C3H

(18)

prominent reactions are dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a

dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a "clean" feedstock

molecular hydrogen. Therefore, dehydrogenation reactions will proceed only if the catalyst is contaminated with

Page: 152

Transalkylation Cyclization Dealkylation Dehydrogenation Polymerization Alkylation Specific Reaction n-C10H22 -> n-C7H16 +

Page: 340

catalyst, promoting undesirable dehydrogenation and condensation reactions. These nonselective reactions increase gas and coke

Page: 381

Nickel, 63, 108 dehydrogenation, 135 and hydrogen, 64 passivation, 122 Nitrogen basic, 54 effects,

Page: 382

3§7 dehydrogenation, 135 hydrogen transfer, 134 isomerization, 133 thermal cracking, 126, 283

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File

:

Organic_Chemistry.pdf

Title

:

Subject

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:

Keywords :

Page: 811

the product of dehydrogenation of the natural product guaiol with elemental sulfur. From the

Page: 1095

RNH2 PThis dehydrogenation is the reverse of palladium-catalysed hydrogenation. NH2 HN R

Page: 1289

of FAD involve dehydrogenations—as in double bond formation from single bonds. Of course,

Page: 1312

a sulfur-promoted dehydrogenation has been suggested for the removal of the hydrogen atoms.

(20)

File

:

Renewable_Energy_3E_.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 507

second stage involves dehydrogenation (removing hydrogen atoms from the biomass material), such as

Page: 508

4.152) followed by dehydrogenation: 2C2H5OH + CO2 → 2CH3COOH + CH4 (4.153) The

Page: 571

of hydrogenation and dehydrogenation multistage adia5.2 ENERGY STORAGE 553

Page: 572

nitrogen in the dehydrogenation and hydrogen in the hydrogenation units. A number of ammoniated

(21)

File

:

BRETHERICK_Handbook_Reactive_Chemical_Hazards_6E_VOLUME1.pdf

Title

:

Subject

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Author

:

Keywords : Referex

Page: 628

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File

:

Chemical_Process_Equipment.pdf

Title

: Chemical Process Equipment Selection and Design

Subject

:

Author

: Stanley M. Walas

Keywords : Referex

Page: 585

is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page: 586

catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids

4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included

combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page: 587

13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and

are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page: 588

for hydrodealkylatisn and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page: 595

operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

(23)

File

:

84607_01.pdf

Title

: c01 1..44

Subject

:

Author

:

Keywords :

Page: 31

intermediate reduction step. Dehydrogenation of the alcohol to the aldehyde is followed by aldol

(24)

File

:

84607_16.pdf

Title

: c01 1..60

Subject

:

Author

:

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Page: 13

procedure, desaturation or dehydrogenation, offers more attractive prospects. Flavor deterioration in fat-rich milk

(25)

File

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84607_32.pdf

Title

: c03 49..66

Subject

:

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:

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Page: 10

be explained by dehydrogenation and rearrangement of a- and g-terpinene, and hydrogenation and

(26)

File

:

84607_41.pdf

Title

: c12 319..360

Subject

:

Author

:

Keywords :

Page: 12

lycopene by hydrogenation, dehydrogenation, cyclization, and oxidation, or a combination of these processes (

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File

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84607_80.pdf

Title

: c08 279..306

Subject

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:

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Page: 11

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File

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84607_81.pdf

Title

: c09 307..352

Subject

:

Author

:

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Page: 9

(29)

File

:

Instrumentation_Reference_Book_3E.pdf

Title

: Instrumentation Reference Book Third Edition

Subject

:

Author

: Walt Boyes

Keywords : Referex

Page: 217

co-doping and dehydrogenation of the fiber to increase its photosensitivity. Gratings have also

(30)

File

:

Rules_of_Thumb_for_Chemical_Engineers_3E.pdf

Title

: RULES OF THUMB FOR CHEMICAL ENGINEERS

Subject

:

Author

: CARL BRANAN

Keywords : Referex

Page: 226

proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page: 271

development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional

hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

(31)

File

:

M26.pdf

Title

: Section 26 — Members

Subject

:

Author

:

Keywords :

Page: 11

Quorum & Associates DEHYDROGENATION SYSTEMS Aker Kvaerner, Inc. CB&I Howe-Baker Process &

(32)

File

:

J.G.Speight - Chemical and process design handbook.pdf

Title

:

Subject

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Author

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Keywords :

Page: 4

Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

Page: 27

DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of

as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH

that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen.

very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig.

from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page: 28

distillation follows. The dehydrogenation of paraffins yields detergent alkylates and n-olefins. The

rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of

recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

Page: 43

higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page: 44

desired temperature. See Dehydrogenation.

Page: 74

alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

(33)

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

Page: 153

and by the dehydrogenation of butane or the butenes using an iron oxide (

Page: 158

to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain

both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia

pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page: 160

butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page: 176

this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

Page: 270

through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to

2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

Page: 302

oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

Page: 315

is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

Page: 331

hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page: 338

produced by the dehydrogenation of iso-pentane in the same plant used for the

Page: 353

(34)

Page: 422

nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

Page: 440

such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

Page: 548

from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as

H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page: 561

are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page: 565

oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

Page: 582

yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the

cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

Page: 627

of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

(35)

File

:

Applied_Process_Design_VOLUME1_3E.pdf

Title

: APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL

PLANTS, Volume 1, 3rd Edition

Subject

:

Author

: Ernest E. Ludwig

Keywords : Referex

Page: 542

(36)

File

:

F585A1265F4FE23F5629236910CA9E78.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 9

which decreases the dehydrogenation poisoning activity of Ni and V. The catalytic cracker is reforming reaction is dehydrogenation of naphthenes, or removal of hydrogen from the molecule. Important

(37)

File

:

Coulson_Richardsons_Chemical_Engineering_Volume_2.pdf

Title

:

Subject

:

Author

:

Keywords : Referex

Page: 568

(38)

File

:

Rules_of_Thumb_for_Chemical_Engineers_3E.pdf

Title

: RULES OF THUMB FOR CHEMICAL ENGINEERS

Subject

:

Author

: CARL BRANAN

Keywords : Referex

Page: 226

proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page: 271

development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional

hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

(39)

File

:

Renewable_Energy_3E_.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 507

second stage involves dehydrogenation (removing hydrogen atoms from the biomass material), such as

Page: 508

4.152) followed by dehydrogenation: 2C2H5OH + CO2 → 2CH3COOH + CH4 (4.153) The

Page: 571

of hydrogenation and dehydrogenation multistage adia5.2 ENERGY STORAGE 553

Page: 572

nitrogen in the dehydrogenation and hydrogen in the hydrogenation units. A number of ammoniated

(40)

File

:

Chemical_Process_Equipment.pdf

Title

: Chemical Process Equipment Selection and Design

Subject

:

Author

: Stanley M. Walas

Keywords : Referex

Page: 585

is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page: 586

catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids

4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included

combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page: 587

13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and

are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page: 588

for hydrodealkylatisn and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page: 595

operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

(41)

File

:

677rev.pdf

Title

: Microsoft Word - 677rev.doc

Subject

:

Author

: Administrator

Keywords :

Page: 3

a set of dehydrogenation and cyclization reactions finally yielding a graphitic coke layer. Several

(42)

File

:

Borsa_20PhD_20Thesis_20Defense.PDF

Title

: Defense

Subject

:

Author

: Tom McKinnon

Keywords :

Page: 23

(43)

File

:

ccl4 effect on pyrolysis reaction.pdf

Title

: No Job Name

Subject

:

Author

:

Keywords :

Page: 3

(44)

File

:

coking.pdf

Title

: Defense

Subject

:

Author

: Tom McKinnon

Keywords :

Page: 23

(45)

File

:

Experiments in Catalytic Reaction Engineering (J. M. Berty).pdf

Title

: Experiments in Catalytic Reaction Engineering

Subject

:

Author

: J. M. Berty

Keywords : Referex

Page: 60

such as butane dehydrogenation. For exothermic reactions, very small diameter tubes with a single

Page: 165

presented for the dehydrogenation of butane.

Page: 199

for an endothermic dehydrogenation in the synthetic rubber program during World War 11 were

Page: 202

vehicle fLels. Ethylbenzene dehydrogenation to styrene is another example. On Figure 8.:2.2 the

(46)

File

:

Fluid catalytic cracking Handbook.pdf

Title

: 92155.pdf

Subject

:

Author

:

Keywords :

Page: 77

reactions, such as dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation

dehydrogenation and condensation. Dehydrogenation means the removal of hydrogen; and condensation means polymerization,

Page: 78

matrix. Nickel promotes dehydrogenation reactions, removing hydrogen from stable compounds and making unstable olefins,

Page: 79

activity to promote dehydrogenation reactions, A small amount of nickel in the FCC feed to increase the dehydrogenation reactions. Chlorides in the feed reactivate aged nickel, resulting in

an indicator of dehydrogenation reactions. However, the ratio is sensitive to the reactor temperature

Page: 80

Vanadium also promotes dehydrogenation reactions, but less than nickel. Vanadium"s contribution to hydrogen yield

Page: 119

indicative of the dehydrogenation activity of the metals on the catalyst. The addition of

Page: 123

catalyst. They cause dehydrogenation reactions, which increase hydrogen production and decrease gasoline yields. Vanadium

Page: 137

with nickel, the dehydrogenation reactions that are

Page: 141

7. 8. Naphthenes Dehydrogenation Dealkylation Condensation C7H14 - n-C8H18 lso-C3H Ar-C3H

(47)

prominent reactions are dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a

dehydrogenation and coking. Dehydrogenation. Under ideal conditions (i.e., a "clean" feedstock

molecular hydrogen. Therefore, dehydrogenation reactions will proceed only if the catalyst is contaminated with

Page: 152

Transalkylation Cyclization Dealkylation Dehydrogenation Polymerization Alkylation Specific Reaction n-C10H22 -> n-C7H16 +

Page: 340

catalyst, promoting undesirable dehydrogenation and condensation reactions. These nonselective reactions increase gas and coke

Page: 381

Nickel, 63, 108 dehydrogenation, 135 and hydrogen, 64 passivation, 122 Nitrogen basic, 54 effects,

Page: 382

3§7 dehydrogenation, 135 hydrogen transfer, 134 isomerization, 133 thermal cracking, 126, 283

(48)

File

:

BRANAN, C. R. (2002). Rules of Thumb for Chemical Engineers (3rd

ed.).pdf

Title

: RULES OF THUMB FOR CHEMICAL ENGINEERS

Subject

:

Author

: CARL BRANAN

Keywords : Referex

Page: 226

proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page: 271

development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional

hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

(49)

File

:

Chemical Reaction Engineering & kinetics.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 28

independent equations. The dehydrogenation of ethane (C,H,) is used to produce ethylene

Page: 106

1) Dehydration and dehydrogenation of C$H,OH VV QH,OH + GH, +

Page: 124

metal catalyst favors dehydrogenation of an alcohol to an aldehyde, but an oxide catalyst

Page: 134

‘In the dehydrogenation of &He to produce CzH4, CH4 is a minor

Page: 156

in the ethane dehydrogenation mechanism of Section 6.1.2: Ho + C,H; + C,

Page: 157

rate of ethane dehydrogenation. These and similar reactions have a substantial influence in reactions

Page: 172

process like ethane dehydrogenation, where detailed molecular models of the free-radical chemistry are

Page: 183

kinetics of ethane dehydrogenation to produce ethylene, the relatively simple mechanism given in Section

Page: 190

6.1.2 for the dehydrogenation of CzH6, obtain the rate law for CzH6 + Cz&

Page: 191

11 on the dehydrogenation of ethane to produce ethylene. It can be treated as

(50)

good hydrogenation and dehydrogenation catalysts. (7) Although it may be correct to say

Page: 234

and subsequently catalyze dehydrogenation reactions. In this case, the yield of gasoline is reduced,

Page: 238

kinetics of ethanol dehydrogenation over Cu in the presence of water vapor, acetone, or

Page: 295

S) by a dehydrogenation reaction catalyzed by yeast alcohol dehydrogenase (YADH). Nikolova et

Page: 304

Examples are the dehydrogenation of C,H6 to produce C,H, (noncatalytic, low

Page: 384

such as the dehydrogenation of ethane for production of ethylene, take place in such

example, in the dehydrogenation of ethylbenzene for the production of styrene monomer, or in

Page: 385

as in the dehydrogenation of ethane to ethylene. We consider next the three types

Page: 397

Nonisobaric Operation The dehydrogenation of ethane (A) to ethene (B) is conducted

Page: 445

which may undergo dehydrogenation to form benzene and isomerization to form methylcyclopentane, as follows:

Page: 531

styrene monomer by dehydrogenation of ethylbenzene: CsH,, * CsH, + H, (W This

Page: 538

we use the dehydrogenation of ethylbenzene, reaction (D) in Section 21.1. This is example. For the dehydrogenation of ethylbenzene at equilibrium, CsH,, (EB) + CsH, (

Page: 540

such as the dehydrogenation of ethylbenzene), as also shown in Section 5.3 and illustrated

Page: 549

(51)

involving only the dehydrogenation reaction ((D) in Section 21.1), and use the kinetics

Page: 565

stages, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer), a) For the dehydrogenation of ethylbenzene (A), reaction (D) in Section 21.1,

Page: 566

flow, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer). flow, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer). flow, for the dehydrogenation of ethylbenzene (A) to styrene (S) (monomer).

Page: 682

517,574,575 Ethane, CzH,+ dehydrogenation, 35-36,154,286,366, 376-377,379-380 mechanism, 116,124-125,137,138-139,158

165,172,173-314,445 Ethylbenzene, CsHrs: dehydrogenation to styrene, 176,366,513,522 equilibrium considerations, 520-521,522, 547 reactor calculations,

Page: 685

273,275 for ethane dehydrogenation, 116,124-125, 137,138-139,158,165,172,173-175 for formation of HBr,

(52)

160-File

:

Chemical Reactor Design Optimization & Scaleup - Nauman.pdf

Title

: 3799-nauman-pre 1..14

Subject

:

Author

:

Keywords :

Page: 121

for the catalytic dehydrogenation of ethylbenzene to form styrene: C8H10 !C8H8

Page: 145

favorable equilibrium. Ethylbenzene dehydrogenation fits this situation. Repeat Problem 3.7 but substitute an annular

Page: 263

HR for the dehydrogenation of ethylbenzene to styrene at 298.15K and 1 bar. Solution:

Page: 264

for the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. Solution: From Example 7.8,

Page: 265

R for the dehydrogenation of ethylbenzene to styrene at 298.15 K. Solution: Table 7.2

Page: 272

of the ethylbenzene dehydrogenation reaction at 298.15K and 0.5 atm. Consider two cases: 1.

Page: 273

from the ethylbenzene dehydrogenation reaction at 973K and 0.5 atm. The starting composition is

amount of a dehydrogenation catalyst. The reaction rate has the form kf A

Page: 274

trajectory for ethylbenzene dehydrogenation.

Page: 394

process for the dehydrogenation of ethylbenzene uses 3-mm spherical catalyst particles. The rate

Page: 407

(53)

constant of 3.752

Page: 410

(54)

File

:

Chemical.Process.and.Design.Handbook.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 4

Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

Page: 27

DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of

as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH

that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen.

very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig.

from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page: 28

distillation follows. The dehydrogenation of paraffins yields detergent alkylates and n-olefins. The

rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of

recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

Page: 43

higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page: 44

desired temperature. See Dehydrogenation.

Page: 74

alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

(55)

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

Page: 153

and by the dehydrogenation of butane or the butenes using an iron oxide (

Page: 158

to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain

both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia

pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page: 160

butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page: 176

this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

Page: 270

through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to

2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

Page: 302

oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

Page: 315

is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

Page: 331

hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page: 338

produced by the dehydrogenation of iso-pentane in the same plant used for the

Page: 353

(56)

Page: 422

nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

Page: 440

such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

Page: 548

from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as

H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page: 561

are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page: 565

oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

Page: 582

yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the

cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

Page: 627

of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

(57)

File

:

Cheremisinoff - Pressure Safety Design Practices for Refinery and Chemical

Operations.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 21

cracking, isomerization, alkylation, dehydrogenation, etc., taking place in a cat reactor, they are complicated,

Page: 99

as feedstock for dehydrogenation to butadiene. The rich acid extract is flashed to about

Page: 100

1-butenes for dehydrogenation feed, the isobutylene dimer being added to the motor gasoline

Page: 102

isobutylene extraction, butene dehydrogenation, or used in further refinery processing. Isoprene The demand for

Page: 106

from Ethylbenzene by Dehydrogenation Ethylbenzene is dehydrogenated to styrene over a fixed bed of

(58)

File

:

Ed Peters and Timmerhaus - Plant Design and Economics for Chemical

Engineer - 4th Edition.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 20 by catalytic t dehydrogenation of Page: 855

produced by the dehydrogenation of isopropanol according to the following reaction: CH3\ /H

Page: 880

production by catalytic dehydrogenation are to be analyzed with respect to three variables. These

(59)

File

:

Ludwig

-Applied_Process_Design_For_Chemical_And_Petrochemical_Plants__Volume_1

3rd Ed 1999.pdf

Title

: APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS,

Volume 1, 3rd Edition

Subject

:

Author

: Ernest E. Ludwig

Keywords : Referex

Page: 543

(60)

File

:

Ray & Johnston - Chemical Engg Design Project A Case Study

Approach.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 368

of acetone. Catalytic dehydrogenation of ethyl benzene. Hydrochlorination of methanol. Catalytic dehydrogenation of

n-of methanol. Catalytic dehydrogenation n-of n-butenes; feedstock n-of liquid mixed hydrocarbon stream containing

(61)

File

:

Coulson_Richardsons_Chemical_Engineering_Volume_2.pdf

Title

:

Subject

:

Author

:

Keywords : Referex

Page: 568

(62)

File

:

Soares - Process Engineering Equipment Handbook - 2002.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 1220

of naphthenes through dehydrogenation and of paraffins through isomerization and dehydrocyclization. The reformer catalyst,

reformers do. The dehydrogenation and dehydrocyclization reactions produce large amounts of hydrogen as a

(63)

File

:

Speight - Chemical Process & Design Handbook - 2002.pdf

Title

: Microsoft Word - Doc1.doc

Subject

:

Author

: a

Keywords :

Page: 5

Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

Page: 28

DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of

as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH

that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen.

very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig.

from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page: 29

distillation follows. The dehydrogenation of paraffins yields detergent alkylates and n-olefins. The

rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of

recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

Page: 44

higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page: 45

desired temperature. See Dehydrogenation.

Page: 75

alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

(64)

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

Page: 154

and by the dehydrogenation of butane or the butenes using an iron oxide (

Page: 159

to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain

both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia

pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page: 161

butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page: 177

this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

Page: 271

through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to

2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

Page: 303

oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

Page: 316

is formed by dehydrogenation of pyridine and quaternization with ethylene dibromide. 2.257

Page: 332

hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page: 339

produced by the dehydrogenation of iso-pentane in the same plant used for the

Page: 354

(65)

Page: 423

nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

Page: 441

such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

Page: 549

from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as

H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page: 562

are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page: 566

oxide and nonylphenol. Dehydrogenation of n-alkanes from petroleum (C9H20

Page: 583

yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the

cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

Page: 628

of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

(66)

File

:

Walas - Chemical Process Equipment - Selection and Design - 1990.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 581

is a suitable dehydrogenation accelerator; the most favorable temperature will be different for each

Page: 582

catalysts. They catalyze hydrogenationdehydrogenation as well as many of the reactions catalyzed by acids

4. Dehydration and dehydrogenation combined utilizes dehydration agents combined with mild dehydrogenation agents. Included

combined with mild dehydrogenation agents. Included in this class of catalysts are phosphoric acid,

Page: 583

13. Hydrogenation and dehydrogenation employ catalysts that form unstable surface hydrides. Transition-group and

are the hydrogenation-dehydrogenation component of the catalyst and alumina is the acid component

Page: 584

for hydrodealkylation and dehydrogenation reactions Palladium-on-alumina catalyst, for selective hydrogenation of acetylene

Page: 592

operation feasible; butane dehydrogenation, for example, is done this way. Because of their long

Page: 597

from ethanol 18. Dehydrogenation of isopropanol 19. Isomerization of n-butane 20. Post-chlorination

(67)

File

:

30A9B8D1823ABBC9E2E9FCF73FB8C717.pdf

Title

: Speight_Part II_K and L

Subject

:

Author

: Systems Administrator

Keywords :

Page: 13

(68)

File

:

3D1619E86AD17469AECBA817225B76E.pdf

Title

: Speight_Part II_A

Subject

:

Author

: Systems Administrator

Keywords :

Page: 15

alcohol by either dehydrogenation (preferred) or air oxidation. These are catalytic processes at

Page: 37

by either partial dehydrogenation to olefins and addition to benzene with hydrogen fluoride (

(69)

File

:

4DFCD212563EFB48B5E607A6D5F081.pdf

Title

: Speight_Part II_H

Subject

:

Author

: Systems Administrator

Keywords :

Page: 2

(70)

File

:

5F8EDEADEA27CB27003EB3C034E9FD.pdf

Title

: Speight_Part II_O&P

Subject

:

Author

: Systems Administrator

Keywords :

Page: 16

such as alkylation, dehydrogenation, hydrogenation, and isomerization, are essentially identical to those operations used

(71)

File

:

6DEE225BB9712C11AFAF9D52EC496.pdf

Title

: Speight_Part 1_H

Subject

:

Author

: Systems Administrator

Keywords :

Page: 10

higher temperatures favor dehydrogenation, but the catalysts used are the same as for hydrogenation.

Page: 11

(72)

File

:

83D76FDA28112EDD8B955961C1A2CA7.pdf

Title

: Speight_Part II_S

Subject

:

Author

: Systems Administrator

Keywords :

Page: 38

from ethylbenzene by dehydrogenation at high temperature (630oC) with various metal oxides as

H2 Most dehydrogenations do not occur readily even at high temperatures. The driving

Page: 51

are prepared by dehydrogenation of paraffins, by polymerization of ethylene to a-olefins using

Page: 55

(73)

File

:

9E26C05E48104BE4A1DD16A082955D17.pdf

Title

: Speight_Part II_I

Subject

:

Author

: Systems Administrator

Keywords :

Page: 3

hydrogenation, oxidation, and dehydrogenation. The 1-naphthol is made from naphthalene, which is obtained

Page: 10

(74)

File

:

A6914BED4D79868813A211C6C43902D.pdf

Title

: Speight_Part II_N

Subject

:

Author

: Systems Administrator

Keywords :

Page: 26

nonbiodegradability. Cracking and dehydrogenation of n-paraffins is now the preferred method, giving very

(75)

File

:

AFCDFD46BB6145807DC55AAE2917254D.pdf

Title

: Speight_Part II_E

Subject

:

Author

: Systems Administrator

Keywords :

Page: 7

through a catalytic dehydrogenation reactor where part of the ethyl alcohol is dehydrogenated to

2 Distillation Distillation Dehydrogenation reactorSelective hydrogenation reactor Hydrogen Ethyl acetate Ethyl alcohol Recycle

(76)

File

:

C31E3FD43EAEC5E661CCCB0809A1FB.pdf

Title

: Speight_Part II_B

Subject

:

Author

: Systems Administrator

Keywords :

Page: 29

and by the dehydrogenation of butane or the butenes using an iron oxide (

Page: 34

to tetrahydrofuran. With dehydrogenation catalysts, such as copper chromite, butanediol forms butyrolactone. With certain

both dehydration and dehydrogenation occur, giving 2,3-dihydrofuran. Heating butanediol or tetrahydrofuran with ammonia

pyrrolidines. With a dehydrogenation catalyst, amino groups replace one or both of the hydroxyl

Page: 36

butane. One is dehydrogenation to isobutylene followed by conversion of the isobutylene to the

Page: 52

this material is dehydrogenation of butanediol. The manufacture of butyrolactone by hydrogenation of maleic

(77)

File

:

CC92C94D0E857FDED2FD8AE1840BC97.pdf

Title

: Speight_Part 1_C&D

Subject

:

Author

: Systems Administrator

Keywords :

Page: 3

DEHYDROGENATION Dehydrogenation is a reaction that results in the removal of

as in the dehydrogenation of ethane to ethylene: CH3CH3 → CH

that causes some dehydrogenation, indicated by the presence of unsaturated compounds and free hydrogen.

very large-scale dehydrogenation processes. Styrene is produced from ethylbenzene by dehydrogenation (Fig.

from ethylbenzene by dehydrogenation (Fig. 1). Many lower molecular weight aliphatic ketones are

Page: 4

distillation follows. The dehydrogenation of paraffins yields detergent alkylates and n-olefins. The

rhenium for selective dehydrogenation has increased in recent years since dehydrogenation is one of

recent years since dehydrogenation is one of the most commonly practiced of the chemical processes. See Hydrogenation. DEHYDROGENATION 1.15

(78)

File

:

D6AC68B3AB4D17F98E72EAD2C62EF0B3.pdf

Title

: Index_Speight_HB1 6x9

Subject

:

Author

: Systems Administrator

Keywords :

Page: 4

of alcohol, 1.13 Dehydrogenation, 1.14 catalysts for, 1.1.3 Detergents, 2.190 Dextrose, 1.18 Diallyl phthalate,

(79)

File

:

DE56D48D9A3EB57B869C5B68EF163ACC.pdf

Title

: Speight_Part II_T

Subject

:

Author

: Systems Administrator

Keywords :

Page: 14

yield aromatics are dehydrogenation or aromatization of cyclohexanes, dehydroisomerization of substituted cyclopentanes, and the

cyclopentanes, and the cyclodehydrogenation of paraffins. One toluene production process commences with mixed hydrocarbon

(80)

File

:

F64F21FD3359EE5DD459D678E8FE1218.pdf

Title

: Speight_Part II_F

Subject

:

Author

: Systems Administrator

Keywords :

Page: 10

oxidation or simple dehydrogenation. 2CH3OH + O2 → 2HCH=O + to cause the dehydrogenation to take place. In the process (Figs. 1 and

(81)

File

:

FA94FBA92701ACCC2B7612576CCA134.pdf

Title

: FM_Speight_HB1

Subject

:

Author

: Systems Administrator

Keywords :

Page: 1

Dehydration / 1.13 Dehydrogenation / 1.14 Esterfication / 1.16 Ethynylation / 1.17 Fermentation /

(82)

File

:

PEP Yearbook process list.pdf

Title

: PEP Yearbook process list.xls

Subject

:

Author

: Russell Heinen

Keywords :

Page: 1

BY VAPOR PHASE DEHYDROGENATION ACETONITRILE ACETONITRILE RECOVERY IN ACRYLONITRILE MANUFACTURE ACETYLENE ACETYLENE FROM CALCIUM

Page: 2

BUTENES BY OXIDATIVE DEHYDROGENATION BUTADIENE RECOVERY BY DIMETHYLFORMAMIDE EXTRACTIVE DISTILLATION BUTADIENE RECOVERY BY

N-Page: 5

FROM ETHANE BY OXYDEHYDROGENATION ETHYLENE FROM ETHANE BY CONVENTIONAL CRACKING WITH FRONT-END DEETHANIZATION

Page: 8

BY THE OLEFLEX DEHYDROGENATION PROCESS ISOBUTYLENE FROM ISOBUTANE BY THE SNAMPROGETTI/YARSINTEZ PROCESS ISODECYL

Page: 9

BY VAPOR PHASE DEHYDROGENATION OF METHANOL METHYL ISOBUTYL CARBINOL METHYL ISOBUTYL CARBINOL FROM METHYL

Page: 14

PROPANE BY CATALYTIC DEHYDROGENATION PROPYLENE, POLYMER GRADE, FROM REFINERY GRADE PROPYLENE (66 WT

(83)

File

:

Dipo Baskoro - Prarancangan Pabrik Metil Tersier Butil Eter dari

Isobutylene dan Metanol.pdf

Title

: Microsoft Word - Dipo Baskoro - Prarancangan Pabrik Metil Tersier Butil

Eter dari Isobutylene dan Metanol.doc

Subject

:

Author

: Dipo

Keywords :

Page: 8

Could not extract contextual text. The document has restricted security permissions and content copying is not allowed.

(84)

File

:

Levenspiel O. Chemical reaction engineering (3ed., Wiley, 19.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 513

21.12. In catalytic dehydrogenation of hydrocarbons the catalyst activity decays with use because of

(85)

File

:

Marks.Standard.Handbook.for.Mechanical.Engineers.10th.Editio.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 557

Provide oxygenates Isobutane dehydrogenation Feedstock for oxygenate synthesis Catalytic cracker naphtha fractionation Increase alkylate

(86)

File

:

McGraw-Hill"s Engineering Companion.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 160

balances. The ethanol dehydrogenation reaction is carried out with the feed entering at 300 chart of ethanol dehydrogenation process.

(87)

File

:

Plant Design and Economics for Chemical Engineers (M. S. Pet.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 20 by catalytic t dehydrogenation of Page: 855

produced by the dehydrogenation of isopropanol according to the following reaction: CH3\ /H

Page: 880

production by catalytic dehydrogenation are to be analyzed with respect to three variables. These

(88)

File

:

Rules_of_Thumb_for_Chemical_Engineers.pdf

Title

: RULES OF THUMB FOR CHEMICAL ENGINEERS

Subject

:

Author

: CARL BRANAN

Keywords : Referex

Page: 226

proposed ethyl-benzene dehydrogenation process. Ethylbenzene and steam were fed to the reactor. and

Page: 271

development of butane dehydrogenation, coal conversion, and gas cracking processes in the 194Os, additional

hydrocarbon processing. Butane dehydrogenation plant personnel noted how iron oxide and coke radiated outward

(89)

File

:

10376_05.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 12

(90)

File

:

10376_13.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 20

hydrogen over hydrogenation-dehydrogenation catalysts, which may be supported on alumina or silica-alumina.

Page: 21

a suitable feed. Dehydrogenation is a main chemical reaction in catalytic reforming, and hydrogen

is to promote dehydrogenation and hydrogenation reactions, that is, the production of aromatics,

(91)

File

:

75551_04.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 24

Condensation Dehydrogenation Esterification Halogenation and manufacture of halogens Hydrogenation

(92)

File

:

4CA091E7C4F3F03356F860E0AE64D16A.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 38

cracking, oxidation, alkylation, dehydrogenation, hydration, and chlorination. Most processes use proprietary catalysts to increase

(93)

File

:

7766X_01a.pdf

Title

:

Subject

:

Author

:

Keywords :

Page: 10

fractionation section. The dehydrogenation of isobutane to isobutene is represented by iCH,CH(CH,),

The gas phase dehydrogenation of isobutane to isobutene iC,Hlo 3 iC,H, +

Page: 11

process flowsheet for dehydrogenation of isobutane Mixing Point 4 unknowns (itAl, itBl, it4,

Page: 12

of gas phase dehydrogenation of isobutane before convergence.

Page: 13

of gas phase dehydrogenation of isobutane after convergence. The enthalpy of formation of iC,

(94)

File

:

F585A1265F4FE23F5629236910CA9E78.pdf

Title

:

Subject

:

Author

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which decreases the dehydrogenation poisoning activity of Ni and V. The catalytic cracker is reforming reaction is dehydrogenation of naphthenes, or removal of hydrogen from the molecule. Important

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