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Anaerobic biodegradability of polyvinyl alcohol 总被引:4,自引:0,他引:4
Summary Biodegradability of polyvinyl alcohol (PVA) under anaerobic conditions was demonstrated using anaerobic river sediments and anaerobically treated activated sludge from a sewage treatment plant. PVA having molecular weights of 2000 and 14000 was over 60% biodegraded as determined by TOC. 相似文献
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The action of two classes of pyrethroids on the inhibition of brain Na-Ca and Ca + Mg ATP hydrolyzing activities of the American cockroach 总被引:1,自引:0,他引:1
Ca2+-stimulated ATP hydrolyzing activities (i.e. Na-Ca ATP hydrolysis and Ca + Mg ATP hydrolysis) measured in cockroach brain tissue were highly sensitive to the action of pyrethroid insecticides under in vitro conditions. Non-cyano-containing pyrethroids inhibited Na-Ca ATP hydrolysis to a greater extent than their cyano-containing counterparts. The reverse is true for pyrethroid action on Ca + Mg ATP hydrolysis. Nonmitochondrial Ca + Mg ATP hydrolysis of disrupted synaptosomes was the most sensitive activity examined. Ca2+-stimulated ATP hydrolyzing activities were inhibited in cockroaches poisoned by permethrin in vivo. In vivo poisoning occurred in the presence of a similar amount of bound [14C]permethrin which had been determined to cause a substantial amount of inhibition to Ca2+-stimulated ATP hydrolyzing activities in vitro. 相似文献
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Separation of dilute aqueous butanol and acetone solutions by pervaporation through liquid membranes
A simultaneous extraction-stripping process is proposed for separating volatile products from fermentation broths, it is based on pervaporation through a liquid membrane supported with a hydrophobic porous membrane. The liquid membrane prepared with oleyl alcohol was selected as the most suitable for separating volatile products resulting from acetone-butanol fermentation. The separation performance and stability of the oleyl alcohol liquid membrane were investigated by using dilute aqueous butanol and acetone solutions. The oleyl alcohol liquid membrane was found to be superior by far in both selectivity and permeability of butanol to the better known silicone rubber membrane in its high selectivity for alcohols. Using the oleyl alcohol liquid membrane, the dilute aqueous butanol solutions of around 4 g/L obtained in acetone-butanol fermentation could be concentrated up to 100 times. The stability of this liquid membrane was also quite good as long as the surface tension of the feed solution was less than the critical surface tension of the support membrane. No change in the separation performance was found after the continuous usage in a long period of 100 h. 相似文献
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Takehiro Masumura Daisuke Shibata Takashi Hibino Tomohiko Kato Koichi Kawabe Go Takeba Kunisuke Tanaka Shoji Fujii 《Plant molecular biology》1989,12(2):123-130
Using a rice maturing seed pUC9 expression library, we isolated a cDNA clone corresponding to 10 kDa sulfurrich prolamin by immunoscreening. A longer cDNA clone was obtained from a gtll library by plaque hybridization using this 32P-labeled cDNA as a probe. A polypeptide sequence composed of 134 amino acids was deduced from the nucleotide sequence. A 24 amino acid signal peptide was assigned by computer calculation for the membrane spanning region and Edman sequencing of the purified mature polypeptide. Remarkably, 20% of methionine and 10% of cysteine were found in the mature polypeptide as well as high contents of glutamine, and hydrophobic amino acids. Part of the amino acid sequence was homologous with a conserved cysteine-rich region found in other plant prolamins. Two repeats of amino acid sequence were found in the polypeptide. 相似文献
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The liquid membrane prepared with oleyl alcohol was used in pervaporation of dilute aqueous butanol solutions. The selectivity of this liquid membrane was found to be superior than that of silicone rubber membrane, and the separation factor for butanol was 180. Energy saving effect of pervaporation in butanol purification was investigated by comparing the energies required to purify a butanol solution of 0.5 wt.% in the following three separation systems; a conventional distillation system, a separation system combining pervaporation with distillation, and a pervaporation system using a hydrophobic membrane and a hydrohylic membrane in series. When the pervaporation using oleyl alcohol liquid membrane was employed as a pretreatment process of butanol purification, the energy requirement was found to be around one-tenth of that of conventional distillation.List of Symbols
E
D
MJ/kg
Specific energy requirement of butanol purification by distillation
-
J kg/(m2 · h)
Total permeation flux
-
J
B
kg/(m2 · h)
Permeation flux of butanol
-
P
1, P
2 MPa
Pressure at inlet and outlet of vacuum pump
-
Q kJ/h
Energy transfer rate
-
Q
C
Q
W
kJ/h
Energy consumption rate of condenser and vacuum pump
-
R J/K · mol
Gas constant
-
t, T °C, K
Temperature
-
W-g/h
Mass flow rate of butanol/water binary mixture
-
(W)
F1
,-kg/h
Mass flow rate of aqueous butanol solution
-
(W)
F2
at inlet and outlet of permeation cell
-
W* kJ/mol
Energy requirement of adiavatic expansion
-
X
B
Butanol mass fraction of aqueous butanol solution
-
(X
B
)
F
Butanol mass fraction of aqueous butanol solution supplied into distillation column
-
(X
B
)
F1
Butanol mass fraction of aqueous butanol
-
(X
B
)
F2
solution at inlet and outlet of permeation cell
-
Y
B
Butanol mass fraction in permeate
-
Separation factor of butanol
-
Adiavatic constant 相似文献