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1.
2.
Most oil producing countries have extensive reserves of heavy oil and bitumen. As easily accessible sources of conventional crudes decline, these reserves will become more important in supplementing the energy requirements. Heavy oil and bitumen are highly viscous and contain 3 to 6% sulphur. These objectionable quantities of sulphur must be removed before being acceptable as refinery feedstock. This paper addresses the potential of biological desulphurization of heavy oil and bitumen. The aerobic and anaerobic processes to remove organic as well as inorganic sulphur have been reviewed. To date, most studies were performed with model substrates, particularly dibenzothiophene (DBT) in a synthetic medium. Early work concerned with the isolation of microorganisms, identification and characterization of intermediate metabolites, and the development of growth media. No commercially viable process has emerged since the engineering details of the process have not been addressed conclusively. Due to high utility and catalyst cost conventional hydrodesulphurization processes are reported to be uneconomic in case of high sulphur oils. Microbial desulphurization, on the other hand, appears to be promising due to the inherent low energy requirement. This process may become more attractive by the application of genetically modified bacteria and improvements in bioreactor design. 相似文献
3.
The engineering considerations common to large scale chromatographic purification of proteins are reviewed. A discussion of the industrial chromatography fundamentals is followed by aspects which affect the scale of separation. The separation column geometry, the effect of the main operational parameters on separation performance, and the physical characteristics of column packing are treated. Throughout, the emphasis is on ion exchange and size exclusion techniques which together constitute the major portion of commercial chromatographic protein purifications. In all cases, the state of current technology is examined and areas in need of further development are noted.
The physico-chemical advances now underway in chromatographic separation of biopolymers would ensure a substantially enhanced role for these techniques in industrial production of products of new biotechnology. 相似文献
4.
Summary A simple method is proposed for calculating oxygen pentration depth in immobilized cells by assuming zero order kinetics in the presence of several external oxygen transport resistances. Calculations indicate that typical penetration depths of oxygen for immobilized microbial cells are in the range of 50–200 and those for immobilized or encapsulated animal and plant tissue culture are about 500–1000 . Based on calculations, oxygen transport in microencapsulation and microcarriers for tissue cultures are not transport-limited, but a slight limitation is expected for those in a hollow fiber reactor.Nomenclature as
specific area of a support (cm)
- Bi
Biot number
-
dimensionless
- Cb
oxygen concentration in the bulk liquid (mM)
-
C
b
C
b
*
-Ccr (mM)
- C
b
*
bulk oxygen concentration in equilibrium with air (mM)
- Ccr
critical oxygen concentration (mM)
- Cs
oxygen concentration in the solid phase (mM)
- dp
diameter or thickness of a support (cm)
- Deff
effective diffusivity of oxygen in the solid phase (cm2/s)
- km
membrane permeability of oxygen (cm/s)
- k
m
*
Deff/m
- kLaL
liquid phase mass transfer rate coefficient (1/s)
- ksas
solid phase mass transfer rate coefficient (1/s)
- (OUR)v
volumetric oxygen uptake rate (mmol O2/l)
- p
geometry parameter, p=0 for slab, p=1 for cylinder, p=2 for sphere
- Pd
oxygen penetration depth (cm)
-
P
d
oxygen penetration depth in the absence of external diffusion limitation (cm)
- Q
volumetric oxygen uptake rate,
(mmol O2/l·h)
-
specific oxygen uptake rate (mmol O2gm biomass (dry)·h)
- r
length coordinate (cm)
- rc
oxygen penetration depth for sphere (cm)
-
r
c
rc in the absence of external diffusion limitation (cm)
- r
c
*
oxygen penetration depth for cylinder (cm)
-
r
c
*
r
c
*
in the absence of external diffusion limitation (cm)
- rcom
combined mass transfer rate resistance (s)
- rd
location where Cs becomes zero or Ccr (cm)
- ri
radius of cylinder or sphere, half thickness of slab (cm)
- Usg
superficial gas velocity (cm/s)
- X
cell concentration (g/l)
Greek letters
Thiele modulus, dimensionless
- L, s
liquid and solid phase volume fraction, respectively, dimensionless
-
effectiveness factor
On sabbatical leave from KAIST, Seoul, Korea 相似文献
5.
Summary A general observer-based estimator method is developed and applied for process modelling and monitoring. This parameter estimation
technique was successfully applied to a L-lysine fermentation process. It was a useful tool to detect the effect of major
culture conditions on cell growth and product synthesis. It can also be used for the development of adaptive optimal control
schemes. 相似文献
6.
Gas holdup and overall volumetric oxygen transfer coefficient in airlift contactors 总被引:13,自引:0,他引:13
The two major types of airlift contactors, concentric-tube and external-loop, were investigated for their gas holdup (riser and downcomer) and overall mass transfer characteristics. Results obtained in batch charges of tap water and 0.15 kmol/m(3) NaCl solution are reported for external-loop airlift contactors having downcomer-to-riser cross-sectional area ratios, A(d)/A(r), ranging from 0.11 = A(d)/A(r) = 0.69 and for concentric-tube types in the range 0.13 = A(d)/A(r) = 0.56.The results are compared and contrasted for the two types of airlift contactors and also with corresponding results obtained in a bubble column (A(d)/A(r) = 0). Both the riser gas holdup, (epsilon(G))(r), and the overall volumetric mass transfer coefficient, (K(L)a(D))(T), were found to increase with increasing gas superficial velocity and the corresponding specific gassing power input, (P(G)/V(D))(T). However, at a specified power input both (epsilon(G))(r) and (K(L)a(D))(T) decreased with increasing A(d)/A(r) due to a resultant increase in circulating liquid velocity. Unifying generalized correlations for both types of airlift contactors are given for both (epsilon(G))(r) and (K(L)a(D))(T). These correlations are expected to be applicable as well to continuous-liquid flow bubble columns at comparable liquid velocities. 相似文献
7.
Summary The use of low-pressure steam autohydrolysis in the pretreatment of corn stover and hybrid poplar has been assessed. In terms of yield of prehydrolyzed solids, minimal by-product formation and extent of subsequent enzymatic saccharification, the results of low-pressure steam pretreatment were found to be as good as or better than those reported for more severe pretreatment processes. Almost complete saccharification of the cellulose in the prehydrolyzed biomass solids was obtained within 24h with a commercial cellulase preparation — Celluclast. The presence of grinding elements (glass beads) during the enzymatic hydrolysis was found to increase the extent of saccharification by 40% to 50% over controls without any grinding elements. 相似文献
8.
Macdonald DG Bakhshi NN Mathews JF Roychowdhury A Bajpai P Moo-Young M 《Biotechnology and bioengineering》1983,25(8):2067-2076
Alkali treatment of corn stover improves the avaliability of cellulose and hemicellulose for enzymatic attack. Treatments were carried out for 1 to 60 min at temperatures and NaOH concentrations ranging from 100 to 150 degrees C and 0 to 2%, respectively. Solubilization of the stover and sugar production by enzymatic hydrolysis (Trichoderma viride cellulase) of the solid residue and the dissolved solids were used to measure the effect of caustic treatment. At 150 degrees C and 2% NaOH concentration, 65% of the original stover was dissolved after 5 min and 52% saccharificatin (g sugar/g stover) of the residue and dissolved solids by enzymatic hydrolysis was achieved compared to 20% for untreated corn stover. 相似文献
9.
The frequencies of chromosome aberrations in 135 workers from nuclear-power plants were compared with those in 135 age-matched controls. A total of 135,000 cells was scored. The frequencies of dicentric chromosome were 1.67 × 10−3 in the exposed group and 0.49 × 10−3 in the control group and those of chromosome-type deletion were 3.33 × 10−3 and 1.10 × 10−3, respectively. The frequencies of all types of chromosome aberrations in the exposed subjects were higher than those in the control group, but no significant trend of dose-dependent increase was observed when only the exposed group were considered. Poisson regression analysis, with both exposed and control included, showed that there was a significant association of chromosome aberration with radiation dose and the duration of work, but not with age, smoking habit and alcohol intake. It was also found that recent exposure to radiation, within the last 5 years, had contributed more to the observed chromosome aberration than earlier exposure. 相似文献