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111.
We describe a process for the commercial manufacture of therapeutic grade plasmid DNA. The industrially scaleable unit operations employed in this process are: (i) optimized alkaline lysis; (ii) bag filtration; (iii) expanded bed anion exchange chromatography; (iv) ultrafiltration, and (v) size exclusion chromatography. These steps are scaleable alternatives to current approaches to plasmid DNA isolation such as high speed centrifugation for feedstock clarification and solvent precipitation for plasmid concentration, and an efficient alternative to conventional low through-put packed bed chromatography.The process produces plasmid DNA characterized by low level chromosomal DNA, RNA and endotoxin contamination without the use of flammable solvents or toxic reagents and is suitable for therapeutic administration.  相似文献   
112.
Physical and biochemical comparison has been made of the performance of a simple fluidised bed contactor and a commercial expanded bed contactor, characterised by identical dimensions, and operated at various settled bed heights with two anion exchange adsorbents. The contactors were tested with various feedstocks comprising bovine albumin in the absence and presence of 20 g dry cell weight biomass litre-1. Earlier classification of the simple contactor as a single-stage, well mixed fluidised bed is reviewed. The relative merits of STREAMLINE DEAE and DEAE Spherodex LS as fluidisable, anion exchange adsorbents are discussed.  相似文献   
113.
In this study, we describe the identification of nine novel genes isolated from a unique human first-trimester cDNA library generated from the placental bed. One of these clones, called C2360 and located on chromosome 10q22, was selected as it showed restricted expression in placental bed tissue as well as in JEG3 choriocarcinoma cells with absent expression in adult tissues. We show that the expression is restricted to first-trimester proliferative trophoblasts of the proximal column and show that C2360 is a nuclear protein. No detectable transactivation potential was observed for different domains of the protein. Secondary structure prediction showed that C2360 is a representative member of a eukaryotic family of proteins with a low conservation at the amino acid level, but with strong conservation at the structural level, sharing the general domain (coiled coil 1)-(helix 1)-(coiled coil 2)-(helix 2), or CHCH domain. Each alpha-helix within this domain contains two cysteine amino acids, and these intrahelical cysteines are separated by nine amino acids (C-X(9)-C motif). The fixed position within each helix indicated that both helices could form a hairpin structure stabilized by two interhelical disulfide bonds. Other proteins belonging to the family include estrogen-induced gene 2 and the ethanol-induced 6 protein. The conserved motif was found in yeast, plant, Drosophila, Caenorhabditis elegans, mouse, and human proteins, indicating that the ancestor of this protein family is of eukaryotic origin. These results indicate that C2360 is a representative member of a multifamily of proteins, sharing a protein domain that is conserved in eukaryotes.  相似文献   
114.
A new one-column chromatography process, analogous to a four-zone simulated moving bed (SMB), was presented. The basic principle of the process was identical to that of a four-zone SMB. The process consisted of one chromatographic column and four tanks, instead of the four columns in the four-zone SMB (1-1-1-1), and has been used for the separation of two amino acids, phenylalanine and tryptophan, using an ion exchange resin. The operating parameters for the one-column process and four-zone SMB were obtained from equilibrium theory. Computer simulations were used to compare the performances of the new one column process to that of the general four-zone SMB, using Aspen Chromatography v 11.1. The differences between the one-column and SMB processes in terms of the purities and yields of phenylalanine and tryptophan were less than 4 and about 6%, respectively. The lower purities of the one-column process were due to the loss of the developed concentration profiles in the column when the liquid was stored in tanks. The one-column process gave great flexibility, and would be useful for reconstructing an existing conventional chromatography process to one of a SMB.  相似文献   
115.
Three anion exchanger expanded bed adsorption (EBA) matrices: Streamline DEAE, Streamline Q XL and Q Hyper Z were evaluated with the aid of EFGP from an ultrasonic homogenate of Escherichia coli. Two pH of buffer were tested. Capture was done in an expanded mode whereas elution was done in a packed mode. The same conditions were chosen for evaluation of the three matrices. We observed a loss of EGFP (8-15%) in the through flow fraction especially with the Streamline Q XL matrix, probably due to an aggregation of beads during sample application. The beads of this matrix possess tentacles which probably retain a lot of cellular and molecular debris. The two other matrices gave a good purification of the EGFP (7-15-fold) but the Q Hyper Z matrix appeared to give the best results. It is composed of little size and density beads which lead to a higher exchange surface and then a better mass transfer.  相似文献   
116.
Antifreeze proteins (AFPs) can protect organisms from freezing injury by adsorbing to ice and inhibiting its growth. We describe here a method where ice, grown on a cold finger, is used to selectively adsorb and purify these ice-binding proteins from a crude mixture. Type III recombinant AFP was enriched approximately 50-fold after one round of partitioning into ice and purified to homogeneity by a second round. This method can also be used to purify non-ice-binding proteins by linkage to AFP domains as demonstrated by the recovery of a 50 kDa maltose-binding protein-AFP fusion from a crude lysate of Escherichia coli.  相似文献   
117.
Compared to the conventional microbial and mammalian systems, transgenic plants produce proteins in a different matrix. This provides opportunities and challenges for downstream processing. In the context of the plant host Brassica napus (canola), this work addresses the bioprocessing challenges of solid fractionation, resin fouling by native plant components (e.g., oil, phenolics, etc.), hydrodynamic stability, and resin reuse for expanded bed adsorption for product capture. Plant tissue processing and subsequent protein extraction typically result in an extract with a high content of solids containing a wide particle-size distribution. Without removal of larger particles, the column inlet distributor plugged. The larger particles (> 50 microm) were easily removed through centrifugal settling comparable to that attainable with a scroll decanter. The remaining solids did not affect the column performance. Less than 4% of the lipids and phenolics in the fed extract bound to STREAMLINE trade mark DEAE resin, and this small proportion could be satisfactorily removed using recommended clean-in-place (CIP) procedures. Hydrodynamic expansion and adsorption kinetics of the STREAMLINE trade mark DEAE resin were maintained throughout 10 cycles of reuse, as was the structural integrity of the resin beads. No significant accumulation of N-rich (e.g., proteins) and C/O-rich components (e.g., oil and phenolics) occurred over the same period.  相似文献   
118.
Stability of expanded beds during the application of crude feedstock   总被引:3,自引:0,他引:3  
Expanded bed adsorption is an integrated technology that allows the introduction of a particle containing feedstock without the risk of blocking the bed. Provided a perfectly classified fluidized bed (termed expanded bed) is formed in the crude feed, a sorption performance comparable to packed beds is found. During the application of biomass containing samples to stable expanded beds an increase in bed expansion due to the higher density and viscosity of the feed is encountered. In this article it is investigated whether the expanded bed condition is also fulfilled during the transition in bed expansion from lower to higher density (i.e., from an equilibration buffer to a biomass containing feedstock). Residence time distribution analyses were performed by using model systems and a yeast suspension during this transition phase. It is shown that in systems in which the biomass does not interact with the fluidized stationary phase, the perfectly classified fluidization is maintained also during this transition phase regardless of the type of feedstock. Additional bed expansion takes place in an "ordered" manner without compromising bed stability. In case of biomass/adsorbent interactions, a deterioration in bed stability is found directly when the crude feed is loaded.  相似文献   
119.
This work describes a simple approach to immobilize functionalized colloidal microstructures onto a C(18)-coated SiO(2) substrate via specific or non-specific bio-mediated interactions. Biotinylated bovine serum albumin pre-adsorbed onto a C(18) surface was used to mediate the surface assembly of streptavidin-coated microbeads (2.8 microm), while a bare C(18) surface was used to immobilize anti-Listeria antibody-coated microbeads (2.8 microm) through hydrophobic interactions. For a C(18) surface pre-adsorbed with bovine serum albumin, hydrophobic polystyrene microbeads (0.8 microm) and positively charged dimethylamino microbeads (0.8 microm) were allowed to self-assemble onto the surface. A monolayer with high surface coverage was observed for both polystyrene and dimethylamino microbeads. The adsorption characteristics of Escherichia coli and Listeria monocytogenes on these microbead-based surfaces were studied using fluorescence microscopy. Both streptavidin microbeads pre-adsorbed with biotinylated anti-Listeria antibody and anti-Listeria antibody-coated microbeads showed specific capture of L. monocytogenes, while polystyrene and dimethylamino microbeads captured both E. coli and L. monocytogenes non-specifically. The preparation of microbead-based surfaces for the construction of microfluidic devices for separation, detection, or analysis of specific biological species is discussed.  相似文献   
120.
The bioremediation of aged polychlorinated biphenyl (PCB)-contaminated soils is adversely affected by the low bioavailability of the pollutants. Randomly methylated-beta-cyclodextrins (RAMEB) were tested as a potential PCB-bioavailability-enhancing agent in the aerobic treatment of two aged-contaminated soils. The soils, contaminated by about 890 and 8500 mg/kg of Aroclor 1260 PCBs, were amended with biphenyl (4 g/kg), inorganic nutrients (to adjust their C:N ratio to 20:1), and variable amounts of RAMEB (0%, 0.5%, or 1.0% [w/w]) and treated in both aerobic 3-L solid-phase reactors and 1.5-L packed-bed loop reactors for 6 months. Notably, significant enhancement of the PCB biodegradation and dechlorination, along with a detectable depletion of the initial soil ecotoxicity, were generally observed in the RAMEB-treated reactors of both soils. RAMEB effects were different in the two soils, depending upon the treatment conditions employed, and generally increased proportionally with the concentration at which RAMEB was applied. RAMEB, which was slowly metabolized by the soil's aerobic microorganisms, was found to markedly enhance the occurrence of the indigenous aerobic, cultivable biphenyl-growing bacteria harboring genes homologous to those of two highly specialized PCB degraders (i.e., bphABC genes of Pseudomonas pseudoalcaligenes KF707 and bphA1A2A3A4BC1 genes of Rhodococcus globerulus P6) and chlorobenzoic acid-degrading bacteria as well as the occurrence of PCBs in the water phase of the soil reactors. These findings indicate that RAMEB enhanced the aerobic bioremediation of the two soils by increasing the bioavailability of PCBs and the occurrence of specialized bacteria in the soil reactors.  相似文献   
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