ライフサイエンスコーパス: packed bed

1 the experiments were carried out in a small packed bed.

2 1.0 nL), and flowing the substrate over the packed bed.

3 ermeability compared with spheres in ordered packed beds.

4 sion in the homogeneous bulk region of these packed beds, accounts for less than 30% of the total edd

5 n suspended growth (SGR) and attached growth packed-bed (AGR) anammox reactors after 220 days of oper

6 a pressure drop equation for flow through a packed bed and allows estimation of key design parameter

7 packed bed with that of an inert glass-beads-packed bed as a control to confirm IERB's effectiveness.

8 ster than current best possible fully porous packed bed, assuming that a critical printing size of d(

9 For example, packed bed breakthrough experiments utilizing UMCM-150 f

10 alate) C-CP fiber columns and a conventional packed-bed (C4-derivatized silica) column has been under

11 if only a reduction in the extent of use of packed beds can be realized.

12 In practice, ordered packed beds can only remain physically stable if the par

13 and CNT films can perform as efficiently as packed-bed carbon sorbents.

14 When GONPs were passed through the packed bed column at 10(-2) and 10(-1) M KCl, 5% and 100

15 s preferred as external absorption unit to a packed bed column based on its ease of operation, despit

16 r for the batch type than for the continuous packed bed column reactor.

17 ubstrate solution in batch type and feedback packed bed column reactors and according to turbidity an

18 erformed in saturated porous media through a packed bed column to simulate fate of graphene oxide nan

19 In packed bed column, a bed height, feed flow rate and inle

20 provided for the fact that a microfabricated packed bed column, which is uniformly filled with radial

21 gth and bacterial attachment efficiency in a packed bed column.

22 acid leachate prepared from lignite coal, a packed-bed column loaded with the MESG biosorbent exhibi

23 In packed-bed column reactors, at low linear velocities, th

24 opic parallel plate system and a macroscopic packed-bed column using fluorescently tagged E. coli as

25 The packed-bed column was operated as prescribed by the colu

26 Unlike the packed bed columns and capillary-based column formats, t

27 be strongly improved by changing the current packed bed columns by a bundle of parallel capillary tub

28 aphic experiments on 4 cm long micromachined packed bed columns filled with radially elongated pillar

29 The precatalyst Pd-PEPPSI-IPent loaded onto packed bed columns shows high catalytic activity for the

30 t in oil recovery from hydrocarbon-saturated packed-bed columns as a result of this metabolism.

31 scherichia coli (E. coli) was examined using packed-bed columns in both saturated and unsaturated por

32 the biogenesis of insoluble iron minerals in packed-bed columns results in effective hydrology altera

33 r capillary columns but might play a role in packed-bed columns with low bonded-phase loadings.

34 chnetium-99 detection in water consists of a packed bed containing a mixture of anion-exchange resin

35 it increased retention in the biofilm-coated packed bed: e.g., the attachment efficiency (alpha) of t

36 erical and monodisperse) and (ii) the use of packed bed experiments which do not allow a direct obser

37 volume of the column hardware outside of the packed bed (extra-bed volume) of very small columns is a

38 g arrangement at the column wall is seen for packed beds extruded from large-diameter columns.

39 e immobilized dirhodium catalyst in a simple packed bed flow reactor achieving comparable yields and

40 Herein we demonstrate a packed bed flow reactor capable of achieving highly regi

41 neous catalyst shows stable performance in a packed-bed flow reactor during a week of continuous oper

42 unction photocatalyst generates ethanol in a packed-bed flow reactor with greatly improved conversion

43 Fabrication of capillaries with integral packed beds for the online determination of human cardia

44 mixtures with a series of physisorbents in a packed-bed geometry.

45 l ion exchange chromatography particles in a packed bed in real time.

46 is shown to decrease performance of ordered packed beds in all observed cases, thus we recommend it

47 Although this has proven true for randomly packed beds in the past, we challenge this paradigm for

48 b-second liquid chromatography in very short packed beds is demonstrated as a broad proof of concept

49 DC) electric field is applied to an immersed packed bed, it invokes electrokinetic processes, such as

50 icator of mobile-phase dispersion in ordered packed bed media, including overlapped beds, and is a us

51 -demand generation of NCF(2)R anions using a packed-bed microreactor containing caesium fluoride.

52 flow and the density of active catalyst in a packed-bed microreactor, as well as control over the dyn

53 xidases, then passed directly to a series of packed-bed modules containing different aminating biocat

54 A packed bed of 1-10-microm ambigel particulates in physic

55 ucting a vent 2 cm after the entrance to the packed bed of 5-microm ODS-AQ modified silica.

56 DAC process combining CO(2) adsorption in a packed bed of amine-functionalized anion exchange resins

57 ves flowing of chromatin fragments through a packed bed of antibody-coated beads, followed by vigorou

58 We used a packed bed of microscale silica beads to filter M. smegm

59 of low Reynolds number flow through a random packed bed of nonporous spherical particles.

60 The system features a packed bed of polystyrene beads inside a rectangular gla

61 A-CE), utilizes a short (approximately 5 mm) packed bed of porous silica containing covalently immobi

62 capillary-adhered thin liquid films in a pre-packed bed of undercooled liquid metal particles lead to

63 Packed beds of basalt powder with large specific surface

64 This device comprises two packed beds of microbeads: first, bioconjugated microbea

65 use pumps to force separated plasma through packed beds of parenchymal cells exhibited significant n

66 evant conditions on SWNT transport through a packed-bed of mixed municipal solid waste collectors.

67 compared to that of a conventional, agarose packed bed, pepsin IMER column commonly used in LC-MS ba

68 mal plasma generated in a dielectric barrier packed-bed plasma reactor for the remediation of dichlor

69 and 12 600 g m(-3) h(-1) for the glass beads packed bed, polyurethane (PU) foam biotrickling filters

70 In this manuscript, a flow-based packed bed reactor approach is described that provides e

71 consists of microchannels, which are used as packed bed reactor compartments, filled with superparama

72 s established with the adsorbed GICA using a packed bed reactor during eleven days at 70 degrees C.

73 Using a packed bed reactor filled with the immobilized biocataly

74 served lactate oxidation solely in the first packed bed reactor zone, with propionate and acetate oxi

75 approach based on an immobilized whole cells-packed bed reactor.

76 n of the PBT-2 catalyst in a continuous-flow packed-bed reactor achieved nearly 60000 turnovers with

77 ers presents an alternative to a traditional packed-bed reactor and avoids large pressure drops, whic

78 back-pressure regulators, static mixers, and packed-bed reactors.

79 wastewater (CRW) was performed in a rotating packed bed (RPB) as a promising process for both CO2 fix

80 n of BOF slag coupled with CRW in a rotating packed bed (RPB).

81 nsing mode, the sample is pumped through the packed bed until complete chromatographic equilibrium is

82 No breakdown of the particles in the packed bed was observed.

83 n design which can either be considered as a packed bed with perfectly ordered and uniform flow paths

84 We compared the conductivity of an IERB packed bed with that of an inert glass-beads-packed bed

85 ribution of carbonates varied between powder packed beds with different powder sizes.

86 w characteristics of the magnetically formed packed bed within the channel allow the assay to be carr