книги из ГПНТБ / Хьюитт Дж. Кольцевые двухфазовые течения

39.

Brooke-Benjamin

T .

Shearing

flow

over

a wavy

boundary.—

«J. Fluid Mech.», 1956, p.

8161.

Sprays

formed

by

flashing

liquid

jets.—

«А.

40.

B row n

R .,

Y o rk

J .

L .

I. Ch. E. J.», 49612, v.

, p.

149.

G o v ie r

G . W . The upward ver­

tical

41.

B row n

R .

A .,

S u lliv a n

G .

A .,

flow of

air — water

mixtures. III. Effect of gas phase density on

flow pattern, hold-up and pressure

drop.— «Can

J .

Chem.

Eng.»,

April

1962, p.

62.

D . Air — water

climbing

film

flow in

an

eccentric

42.

B u tterw o rth

annulus. AERE-R 5787.

P .

H .

Physical

rate

processes

in

industrial fer­

48.

C a ld e rb a n k

1958,

v. 36,

p. 443.

air

44.

C a lv e rt

S .,

W illia m s

B .

Upward

co-current

annular

flow

of

and

water

in

smooth

tubes.— «A.

1. Ch.

E. J.»,

1955,

v.

1,

p.

78.

45.

C a rn a v o s

T .

C .

Thin

film

distillation.— In:

Paper

presented

46.

C arp en ter

F .

G . Ph. D. Thesis. 1948,

Univ. of Delaware.

tic

47.

C a s a g ra n d e

1., C ra v a ro lo

L .,

H a ssid

A . Researches on adiaba­

two-phase

flow.— «Energia

Nueleare»,

4962,

v. 9, p.

148.

48.

C e rm a k

J .

O .,

Jic h a

J .

J . ,

L ig h tn e86r R .

G .

Two-phase

pressure

drop across vertically mounted thich plate

restrictions.— «J.

Heat

Transfer. Trans. AS ME,

Ser. C»,

1964, v.

,

p. 227—239.

49.

C h a m b e rla in

A .

C . Transport of particles across boundary

layers.

1962, AERE-M

1122.

film

50.

C h a rv o n ia

D .

A .

A study of the mean thickness of the liquid

and

the

characteristics

of

the

interfacial

surface

in

annular

two-phase flow in a vertical pipe. 1959, Jet

Propulsion

Center

Report

№-1-59-1. 1959.

D .

A .

An experimental investigation of the mean

51.

C h a rv o n ia

liquid

film

thickness

and

the

characteristics

of the

interfacial

surface

in annular two-phase flow.

1961,

ASM E

Paper

64-WA-24Q.

regimes

in

52.

C h a u d h ry

A .

B .,

E m erton

A .

C .,

Ja c k s o n

R .

Flow

Symposium on Two-Phase

Flow.— «Exeter»,

1965,

21—23 June.

in

53.

C h en

J .

C .

Non-equilibrium

inverse

temperature

profile

boiling

liquid metal -two-phase

flow.— «А.

I.

Ch.

E. J.»,

1965,

v.

11,

p.

1445.

J .

C .

Correlation

for

boiling

heat

transfer

to

saturated

54.

C h e n

fluids

in convective

flow.— «Ind. Eng. Chem. Proc. Des. Dev.», 1966,

v. 5(3),

p.

322.

J .

M .,

M a rtin

W .

Turbulent

two-phase

flow.—

55.

C h en ow eth

M.

«Pet. Ref.», 1955, v. 34(10), p. 151.

and

liquid

film

thickness

56.

C h ien

S .- F .,

Ibele

W .

Pressure drop

of two-phase

annular

and

annular-mist

flows,

1955,

ASM E

Paper

62-WA-170.

G .

H .,

C o lb u rn

A .

D . Mass transfer (absorption)

57.

C h ilto n

coefficients.— «Ind.

Eng.

Ghem.»,

1934, v.

26,

p.

1483.

through

58.

C h ish o lm

D .

The

flow

of

steam — water

mixtures

sharp — edge orifices.— «Engng. Boiler House

Rev.»,

1958, v. 73, p. 252.

fer

59.

C h ish o lm

D .,

P ro v a n

T . F . A

review of heat and mass trans­

during

condensation

in

surface

heat

exchangers.

1963,

D SIR,

Report № 96.

D .,

W atso n

G .

G . The flow of steam — water mixtures

60.

C h ish o lm

two-phase film flow in a vertical

tube. Thesis.

1949,

Univ.

of

Delaware.

A . E. Fluid mechanics

and heat transfer in falling

film

97. D u k le r

system:— In: Paper

presented at

the

ASM E — AlChE

3rd

Nat. Heat

Transfer Conf., August 19Ѳ9.

of

theoretical

and

experimental

film

98. D u k le r

A .

E.

Comparison

thickness. January

86

1961, p. .

P . Characteristics of flow

in

falling

99. D u k le r

A .

E .,

B e rg lin О .

liquid films.— «Chem. Eng. Prog.»,

1952, v. 48,

p.

557.

drop

and

100. D u k le r

A .

E .,

W ick s—6M .,

C le v e la n d

R .

Pressure

hold-up in two-phase

flow.— In:

Paper presented

at

A.

I.

Ch. E.

meeting held Chicago, 4962, 2

December.

probe

for

measu­

101. D u sso u rd

J.

L .,

S ch a p iro

H .

A Deceleration

102.

Ellis

S.

R .

M .,

G a y

B .

The parallel

flow of two fluid stre­

am s— interfacial

shear

and

fluid — fluid

interaction.— «Trans.

Inst..

Chem. Eng.», 1969, v. 37, p. 206.

of

heat

from condensing;

103.

Espig

H .,

H o y le

R .

The transfer

steam

to

a cooled

rotation

disc.— «Trans.

Inst.

Mech.

Eng.»,

1967,,

V. 182,

pt 3H,

p.

1.

two-phase, steam — water flows.— In: Proc..

104.

Fauske H . Critical,

of the 1961 Heat Transfer and Fluid Mech.

Inst.,

p.

79.

Stanford'

Univ. Press, Stanford, California.

105.

Fauske H . K . A theory for predicting pressure gradients for

two-phase critical

flow.— «Nuclear Sei. Eng.»,

1963,

v. 17, p.

1.

106.

F a u sk e

H . K. Two-phase twoand

one-component critical'

flow. Symposium

on

two-phase

Flow.— «Exeter»,

1965,

21—23

June.

107.

Fauske

H. K. Critical flow and the velocity

of

sound

in

two-phase one-component droplet flow.— In:

Paper

presented

at

the

16th Canadian

Chem. D Engng..

Conf. of the Chem.

Inst,

of

Canada,

Windsor,

Ontario, OctoberE.

1966.

piping

compo­

108.

F itzsim m o n s

Two-phase pressure drop in

nents. 1964, HW -80970 Rev. 1.

R .

H . Pressure

drop

characteristics

for

109.

F o r g a n

R .,

W h ittle

channels. 1966, AERE-M 1739.

N .

Dynamics

of

vapor

bubbles

and

110.

F o rste r

H .

K .,

Z ub er

boiling heat transfer.— «А. I. Gh.

E.

J.»,

1955.

and drop

size

of

111.

F ra se r R .

P .,

E ise n k fa m

P .

Liquid atomisation

sprays.— «Trans.

Inst.

Chem.

Eng.»,

1956,

v.

34,

p.

294.

Press,

М 2 .

F ren k el

J .

Kinetic

theory

of liquids. Oxford,

Clarendon

1946.

F re id la n d e r

S .

K .,

Jo h n s to n e

H .

F .

Deposition

of

suspended

113.

particals

from

turbulent

gas stream.— «Ind. Eng. Chem.»,

1957,

v. 49,

p.

1151.

G a d d is

E .

S .,

H a ll

W .

B .

The

equilibrium

of

a

bubble

nucle­

us

1

114.

at

a solid

surface.— «Trans. Inst. Mech. Eng.»,

1967,

v. 182,

pt. 3H,

p.

.

115.

G a le g a r

W .

C .,- S t o v a ll

W .

B .,

H u n tin g to n

R .

L .

More

data

on two-phase vertical

flow.— «Pet.

Ref.»,

1954,

v. 33,

p. 208.

4,

116.

G a rd in e r

J .

A .

Measurement

of

the

drop

size

distribution in

water

sprays

by

an

electrical

method.— «Instrument

Practice»,

196

V.

18,

p.

353.

G .

C .

Events

leading

to erosion

in

the

steam

tur­

117.

G a rd n e r

bine.— «Proc.

Inst. Mech.

Eng.»,

1963,

v.

178,

pt

I,

№

23.

tion

118.

G a rn e r F .

H .,

E llis S .

R .

M .,

L a ce y

J . A .

The

size distribu­

and

entrainment

of

droplets.— «Trans.

Inst.

Chem. Eng.»,

1954,

v.

32,

p.

222.

E .,

R ohrer

W . M .

Sudden

contraction

losses in two-

119.

G e ig e r G .

phase

flow.— «J. Heat Transfer»,

1966, February, p. 1.

spray

ana­

120.

G e is t

J .

M .,

Y o rk

J .

L .,

B row n

G .

G .

Electronic

lyser

for

electrically

conducting

particles— «Ind.

Eng.

Chem.»,

1951,

V.

43,

p .

1371.

L .

E.,

H e w itt

G .

F .

Sampling

probe

studies

of the

gas

Core

121.

G ill

in

droplet

flowrate

after

injection

through

an

axial

jet.

1966.

AERE-M

1202.

122.

G ill

L .

E .,

H ew itt

G . F .,

Lacey P .

JVL C .

Data on

the

up­

wards

annular flow

of

air — water

mixtures.— «Clieni. ling. Sei.», 1962,

V. 20,

p.

71.

L .

E .

a.

oth.

Sampling probe

studies

of the

gas

core

123.

G ill

velocity

distribution.— «Chem.

Eng.

Sei.»,

1963,

v.

18, p. 525.

124.

G ill L . E ., H ew itt G .

E .,

L a ce y

P . M .

C .

Sampling probe

effect of

phase flowrates

on

phase

and

velocity

distribution.— «Chem.

Eng. Sei.», 1964, V . 19,

p .

665.

Physical

Chemistry.

2nd ed. Lon­

125.

G la ssto n e S .

Textbook of

don, MacMillan, 1948, p.

495.

D o rsch

R .

G .

Local

heat

transfer coeffi­

126.

G o o d y k o o n tz

J .

H .,

127.

G o u se

S . W . An index to the two-phase

g a s — liquid flow lite­

gas — liquid flow lite­

128.

G o u se

S . W . An index to the two-phase

rature. Pt II, 1964, MIT Report DSR,

8734-4.

oscillations

in a

closed

129.

G o u se

S .

W .,

A n d ry sia k

C .

D .

Flow

loop with

transparent

parallel

vertical

heated

channels.

1963.

MIT

Report 8973-2.

S . W .,

B row n

G .

A . A survey

of

the velocity of

sound

130.

G o u se

in two-phase mixtures.

1964.

ASM E

Paper

64—WA/F.E-35.

131.

G o u se

S . W ., D ick so n

A . J . The

evaporator tube — state of the

art. M IT

Eng., M IT,

1965.

W .,

H w a n g

С . C .

Visual study of two-phase

one

132.

G o u se

S .

component

flow in a

vertical

tube

with

heat

transfer.

1963.

MIT

Report 8973-1.

G .

W .,

R a d fo rd

B .

A .,

D u n n

J .

S . C . The upwards

133.

G o v ie r

vertical flow of

air — water mixtures. L

Effect of

air and

water

rates

on

flow

pattern,

hold-up pressure drop.— «Can. J.

Chem. Eng.»,

1957,

v.

35, p.

58.

135.

G reen b erg

surface. 1956. Ph. D. thesis, Purdue Univ.

136.

G r iffith

P .

ted pressure. 1963, ANL-6796.

flow

regime

detection.

1964.

ASM E

137.

G rifith

P .

Two-phase

Paper 64-WA/HT-43.

S n y d e r G . A .Г.The

bubbly-slug

transition in

a high

138.

G r iffith P.,

velocity

two-phase flow. 1964. MIT Report 5003-29 (TID-20947).

139.

Гриф ф итс

П „

У олли с

— «Труды

амер. общ-ва инж.-мех’.

Сер. С. Теплопередача»,

1961, № 3, стр. 99.

140.

G rim le y

S .

formance

of packed

towers. Ph. D.

thesis,

London,

1946.

141.

G uerrieri

S . A ., T a lty

R .

D .

A study

of

heat

transfer to

142.

H ab erstro h

R .

D .,

G r iffith

P .

The

transitions

from

the

annular

to the

slug

flow

regime

in

two-phase

flow.

1964.

Report

№ 5003-28, Mech. Eng. Dept., MIT.

148.

H a lle tt

V .

A .

Surface phenomena causing breakdown of

Heat

Mass. Trans­

fer», 1966, V. 9, p. 283.

S. Waves

in

annular

two-phase

flow.

Ph. D.

144.

H a ll-T a y lo r

N .

thesis,

Cambridge,

1967.

S .,

N ed d erm an

R. M . The coalescence

of

145.

H a ll-T a y lo r

N .

disturbance waves in annular two-phase

flow.— «Ohem.

Eng.

Sei.»,

1968, V. 23, p. 551.

N .

S .,

H ew itt

G .

F .,

L a cey P .

C .

The motion

146.

H a ll-T a y lo r

M.

and

frequency

of

large

disturbance waves in annular two-phase

flow,

of air-water mixtures.— «Ghern.

Eng,

Sei.», 1963,

v.

18,

p. 537.

147.

H a n ra tty

T .

J . ,

E n g en

J .

M .

Interaction

between

a

turbulent'

air stream and a moving

water

surface.— «А. I. Ch. E. J.»,

1957, v. 3.,

p. 299.

H a n ra tty

T .

J.,

H ershm an

T.

J.

Initiation

of

roll

waves.—

148.

V.

«А. I. Ch. E. J.», 1961,

7,

p. 488.

D .

E. Stability

of

the

interface“

149.

H a n ra tty

T .

J . ,

W o o d m a n see

for a horizontal air-liquid flow. Symp. on Two-Phase

Flow.— «Exe­

ter», 1965, 21—23 June,

Paper A l.

W .

Criteria

for

the

breakup

o f

150.

H a rtle y

D .

E.,

M u rg a tro y d

surfaces.— «Int.

J.'.

Heat Mass Transfer», 1964, v. 7, p.

1003.

applica­

tion

151.

H e w itt

G .

F .

Analysis of annular two-phase flow;

of

the Dukler analysis to vertical upward

flow

in

a

tube:.

AERE-R 3680, H. M. S. O, 1961,

heat

transfer

and

152.

H ew itt

G .

F .

Some calculations on hold-up,

nucleation

for

steam — water

flow

in

a

0,4

cm

bore

tube.

19621

AERE-R

3984,

G .

E.

Interpretation of pressure drop data from an

153.

H ew itt

annular

channel., 1964,

AERE-R

4340.

entrainment

studies

in

two-

154.

H ew itt

G .

F .

Photographic

and

phase flow systems. 1964, AERE-R 4683.

burnout

data

in

two-

155.

H ew itt

G. E. A

method

of

representing

phase,

heat

transfer

for

uniformly

heated

round

tubes.

1964.

AERE-R

4643.

G .

F .,

K e a rse y

H .

A .

The

correlation of

critical

heat

flux

156.

H ew itt

for

the vertical flow of water in uniformly heated

tubes, annuli

and rod bundles. 1969, AERE-R 5590.

of

the

liquid'

157.

H ew itt

G .

F .,

L

8a ce y P . M . C . The breakdown

film in annular two-phase flow. AERE-R

4303.

See

also.— «Int. J. Heat

Mass

Transfer»,

1963, v.

, p. 784—791.

The

application

of

the

light1:

158.

H ew itt

G .

F .,

L o v e g ro v e

P .

C .

absorption technique

to

continuous film thickness recording in annu­

lar

two-phase

flow. 1962,

AERE-R

3953.

160. H ew itt G .

F .,

S te v e n s A .

T .

G . Two-phase anular flow o f

air — water mixtures

in

an annulus.

Pt

II. Measurements of the effect

181.

Hsu

in a vertical

tube with heat

addition. 1963, NASA-TN-1564.

182.

Hsu

Y. Y., Simon F.

F., Graham R. VV. Application of hot­

fraction

Meeting,

annulaires disperses. CEN G

Symposium, May 1965.

Isbin

H.

S.,

Moy

J.

E.,

da

Cruz A. J. Two-phase

steam —

185. Isbin

water critical

flow. — «А.

I.

Ch.

E. J.», 1957, v.

3, p.

361.

186.

H.

S.

a. otli.

Two-phase stem-water

pressure drops.

March

1958.— «Nuclear

Engng», Pt

V I.

«Chem.

Eng.

Symp.

Ser.»,

1959, № 23, 55, 75— 84.

187.

Isbin

H.

S.

a.

oth.

Void

fractions

in

two-phase flow___

Isbin

«А. I. Ch. E. J.», 1959, V .

5, p.

427,

188.

H. S. a. oth. A

model for correlating two-phase steam —

water

burnout

heat transfer

fluxes.— «Trans.

ASM E.

Ser. C»,

1961,

V . 28, p.

14Ѳ.

189.

Isbin

H. S. a. oth. Two-phase

steam-water pressure

drops-

for critical

flows.— In:

Inst.

Mech. Eng. Symposium on Two-phase

Fluid

Flow,

7 February

1962, Paper 10.

phase flow patterns. 1964, ANL-6958.

R. B.

199.

Johnson M. A., de la Pena J., Mesler

Bubble

shapes

in nucleate boiling.— «Chem. Eng. Prog. Symp.

Series», 1966,

v. 62,

222.

Lane

W.

Shatter of drops in streams

of air.— «Ind.

Eng.

Lavin

Chem.»,

1951, v. 43, p. 1312.

6

223.

Lee I.

J.,

Young

E.

Heat

transfer

to

evaporating

refrige­

rants in

two-phase flow.— «А. I. Ch. E. J.»,

1965,

v.

11,

№ , p. 1124.

224.

Levy

Turbulent

velocity

profile of

a

vertical

film

flow.—

«Ghem. Eng. Sei.», 1965, v. 20, p. 533.

and

heat

transfer

for

225.

S. Theory of pressure drop

annular

steady state two-phase two-component

flow

in

pipes.— In:

Proc. of

the 2nd Mid-western

Conf. on fluid

Mechanics,

1952,

p.

337.

quids in

high velocity

air streams.— «Ind. Eng.

Chem.»,

1953,

v. 45,

p. 667.

Lottes P. A.

—

«Nuclear

234.

Macbeth R. V.Expansion losses in two-phase flow.

Sei. Eng.», 4961, v. 9, p. 26.

235.

Burnout analysis. Pt 4. Application of a local

conditions hypothesis

to wall data for uniformly

heated

round

tubes

in dropwise

condensation.— «J.

Colloid

Sei.»,

1963,

v.

18,

p. 208.

239.

McManus

H. N.

An experimental investigation of film cha­

racteristics

in horizontal

annular

two-phase flow.

1967,

ASM E

Paper 57-A-l 14.

H.

N.

240.

McManus

An

experimental

investigation

of

liquid

annular

two-phase

flow. OOR Project № 2117, Contract

DA-30-115.

Ord-992,

Interim

Rep. №

1, Cornell

Univ. October

1959.

241.

McPherson G. D.

Private communication.

1966.

Magiros

P.

242.

G.,

Dukler

A.

E. Entrainment

and

pressure drop

in concurent

gas — liquid

flow. II. Liquid property

and

momentum ef­

fects, in

Developments

in

Mechanics.

1961. Plenum

Press,

New York.

during

forced

circulation boiling of water.— «Trans. A. S. M. E.»,

1948, V.

70, p.

695.