1996
DOI: 10.1016/0009-2509(96)00321-1
|View full text |Cite
|
Sign up to set email alerts
|

Secondary drop production in packed-bed coalescers

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1

Citation Types

2
14
0

Year Published

2000
2000
2023
2023

Publication Types

Select...
10

Relationship

0
10

Authors

Journals

citations
Cited by 18 publications
(16 citation statements)
references
References 4 publications
2
14
0
Order By: Relevance
“…The emulsion was continuously forced by a membrane dosage pump. The settled oil was discharged discontinuously through the valve (6). The experiments were carried out in a steady-state regime, which was achieved by preoiling the fibers.…”
Section: Equipment and Operating Proceduresmentioning
confidence: 99%
“…The emulsion was continuously forced by a membrane dosage pump. The settled oil was discharged discontinuously through the valve (6). The experiments were carried out in a steady-state regime, which was achieved by preoiling the fibers.…”
Section: Equipment and Operating Proceduresmentioning
confidence: 99%
“…(Sharifi and Shaw, 1996), addition of flucculants and/or a second buoyant particulate phase (Weiland and McPherson 1979) are not applicable as limitations concerning the utilization of extemai objects and cornplicated structures for settling vessels are encountered particularly in metallurgical applications. Therefore improvements in recovery rates for fine drops must be realized by other techniques.…”
Section: Gas Phasementioning
confidence: 99%
“…The authors showed that the separation efficiency of a polypropylene fiber bed was in the range of separation efficiencies realized with other investigated materials [16]. Possibilities of applying different forms of polypropylene as a filter material are still being in the focus of many researches [17][18][19][20][21][22][23].…”
Section: Introductionmentioning
confidence: 99%