Production of bio-fuels by high temperature pyrolysis of sewage sludge using conventional and microwave heating

The pyrolysis of sewage sludge was investigated using microwave and electrical ovens as the sources of heat, and graphite and char as microwave absorbers. The main objective of this work was to maximize the gas yield and to assess its quality as a fuel and as a source of hydrogen or syngas (H2 + CO). Both gases were produced in a higher proportion by microwave pyrolysis than by conventional pyrolysis, with a maximum value of 38% for H2 and 66% for H2 + CO. The oils obtained were also characterized using FTIR and GC-MS. The use of conventional electrical heating in the pyrolysis of sewage sludge produced an oil that could have a significant environmental and toxicological impact. Conversely, microwave pyrolysis still preserved some of the functional groups of the initial sludge such as aliphatic and oxygenated compounds, whereas no heavy PACs were detected.     

Valorization of cotton stalks by fast pyrolysis and fixed bed air gasification for syngas production as precursor of second generation biofuels and sustainable agriculture

In the present study, the potential of cotton stalks utilization for H(2) and syngas production with respect to CO(2) mitigation, by means of thermochemical conversion (pyrolysis and gasification) was investigated. Pyrolysis was conducted at temperature range of 400-760 degrees C and the main parametric study concerned the effect of temperature on pyrolysis product distribution. Atmospheric pressure, air gasification at 750-950 degrees C for various lambda (0.02-0.07) was also studied. Experimental results showed that high temperature favors gas production in both processes; while low lambda gasification gave high gas yield. Syngas (CO and H(2)) was increased with temperature, while CO(2) followed an opposite trend. By pyrolysis, higher H(2) concentration in the produced gas (approximately 39% v/v) was achieved and at the same time lower amounts of CO(2) produced, compared to air gasification.     

The effects of selected gases on excystation of coccidian oocysts.

The mechanism of CO2 action in changing coccidian oocyst wall permeability was indirectly studied by substituting NO, NO2, N2O, H2S, SO2, CH4, NH3, and 8M urea in place of CO2 in an established excystation procedure. Changes in oocyst wall permeability of Eimeria stiedai, E. bovis, and E. tenella were determined by incubation in test gases and cysteine HCl followed by attempted activation of sporozoites by trypsin and bile and staining of intraoocyst components with methylene blue. The gases CH4, NO2, and N2O were negative for all 3 tests, as were SO2, NH3, and 8M urea which, in addition, were toxic to the oocysts. Both H2S and NO were capable of mimicking the action of CO2 and are related chemically to the reducing agent, and thus tend to underscore its importance in excystation. It now appears that the role of CO2 is that of an allosteric effector enhancing the action of the reducing agent.     

Simultaneous Treatment of Dioxins and Heavy Metals in Tagonoura Harbor Sediment by Two-Step Pyrolysis

This paper describes the simultaneous treatment of PCDD/PCDF and toxic heavy metals contaminated sediment by pyrolysis with emphasis on complete removal and destruction of PCDD/PCDF in Tagonoura harbor sediment during a two-step pyrolysis process. Pyrolysis was conducted at different temperatures and N ₂ gas flow rates. Results showed that almost all PCDD/PCDF (99.998%) can be removed from the sediment by treatment at 800°C for 30 minutes in single-step pyrolysis; however, PCDD/PCDF remained in the gas phase without destruction. Analysis also revealed that some PCDD/PCDF formation occurred during the single-step pyrolysis. However, by the use of two-step pyrolysis, where off-gases from the first furnace are heated at 1000°C, PCDD/PCDF in the final gas effluent was dramatically reduced by a thermal degradation mechanism. Stabilization of toxic heavy metals was also observed. Specifically, their leaching activity drastically decreased with increasing pyrolysis temperature. Significant metal volatilization did not occur. Though the low temperature pyrolysis was effective in removing PCDD/PCDF, the leachability of toxic heavy metals such as Cr and Ni was higher that of 800°C; however, lower than untreated. Two-step pyrolysis at 800°C for 30 minutes in the single-step and 1000°C in the two-step pyrolyzer would be effective for the treatment of sediments contaminated with PCDD/PCDF, toxic heavy metals and organic matters simultaneously.     

Biomass downdraft gasifier with internal cyclonic combustion chamber: design, construction, and experimental results

An exploratory downdraft gasifier design with unique biomass pyrolysis and tar cracking mechanism is evolved at Oklahoma State University. This design has an internal separate combustion section where turbulent, swirling high-temperature combustion flows are generated. A series of research trials were conducted using wood shavings as the gasifier feedstock. Maximum tar cracking temperatures were above 1100°C. Average volumetric concentration levels of major combustible components in the product gas were 22% CO and 11% H(2). Hot and cold gas efficiencies were 72% and 66%, respectively.     

Effects of gasifying conditions and bed materials on fluidized bed steam gasification of wood biomass

The effect of steam gasification conditions on products properties was investigated in a bubbling fluidized bed reactor, using larch wood as the starting material. For bed material effect, calcined limestone and calcined waste concrete gave high content of H(2) and CO(2), while silica sand provided the high content of CO. At 650 degrees C, calcined limestone proved to be most effective for tar adsorption and showed high ability to adsorb CO(2) in bed. At 750 degrees C it could not capture CO(2) but still gave the highest cold gas efficiency (% LHV) of 79.61%. Steam gasification gave higher amount of gas product and higher H(2)/CO ratio than those obtained with N(2) pyrolysis. The combined use of calcined limestone and calcined waste concrete with equal proportion contributed relatively the same gas composition, gas yield and cold gas efficiency as those of calcined limestone, but showed less attrition, sintering, and agglomeration propensities similar to the use of calcined waste concrete alone.     

Total recovery of resources and energy from rice straw using microwave-induced pyrolysis

This article presents the application of microwave-induced pyrolysis to total recovery of resources and energy from rice straw. The microwave power and particle size of feedstock were both key parameters affecting the performance of microwave-induced pyrolysis. Under 400-500W microwave power, the reduction of fixed carbon in the biomass was significant. From the experimental results of specific surface area, zeta potential, and Cu(2+) adsorption, the applications of solid residues in the water and wastewater treatment could be expected. The major compositions in gaseous product were H(2), CO(2), CO, CH(4) of 55, 17, 13, 10vol.%, respectively. The high H(2) content might imply that microwave-induced pyrolysis of biomass waste has the potential to produce the H(2)-rich fuel gas. Alkanes, polars, and low-ringed polycyclic aromatic hydrocarbons were three primary kinds of compounds in the liquid product.     

Low temperature catalytic gasification of pig compost to produce H2 rich gas

The low temperature catalytic gasification of pig compost before and after acid washing was carried out to produce H2 rich gas using a two-stage fixed-bed reactor. Little effect of the minerals on the manure pyrolysis is determined. Under the presence of Ni/Al2O3 catalyst nearly all the tarry matters were cracked into H2, CO, CO2 and residual carbon. High H2 and CO yields were obtained by low temperature catalytic steam gasification. Acid washing results in the decrease in the content of the ease-hydrolyzed organic components, which volatilize at low temperature. The change in the gas yields from the manure during catalytic decomposition is in accordance with its pyrolysis behavior.     

Soil flushing of a sandy loam contaminated with Pb(II), PbS4 (s), PbCO3 (3), or Pb‐Naphthalene: Column results

Column‐scale oil flushing of a sandy loam contaminated with either Pb(II) (500 mg/kg Pb), PbSO₄ (10,000 mg/kg Pb), PbCO₃ (10,000 mg/kg Pb), or Pb‐naphthalene (400 mg/kg Pb, 333 mg/kg naphthalene) was investigated. HCl (0.1 N), EDTA (0.01 M), and CaCl₂ (1.0 M) were selected as the soil‐flushing solutions based on soil‐washing experiments. For the Pb‐only tests, Pb removal efficiencies were 85, 100, and 78% for HCl, EDTA, and CaCl₂, respectively. For PbSO₄ (s), Pb removal efficiencies were 32, 100, and 96% for HCl, EDTA, and CaCl₂, respectively, and for PbCO₃ were 97, 100, and 14% for HCl, EDTA, and CaCl₂, respectively. Larger amounts of flushing solutions were required for the remediation of PbSO₄‐and PbCO₃‐contaminated soils compared with the Pb‐only tests, most likely because of slower dissolution kinetics and the neutralization of HCl by CO₃ ^‐2 For Pb‐naphthalene, Pb removal efficiencies were 78 and 72% for HCl and EDTA, respectively, which compared well with soil‐washing results but were less than those observed in Pb‐only column studies.     

Analysis of histamine and N tau-methylhistamine in plasma by gas chromatography-negative ion-chemical ionization mass spectrometry

Current methods of quantitation of histamine and its major metabolite N tau-methylhistamine are inaccurate and insensitive to the very low concentrations that exist in plasma samples. Therefore, an accurate and sensitive method for quantification in plasma has been developed using the stable isotope dilution assay with negative ion-chemical ionization mass spectrometry. For histamine, after the addition of [2H4]histamine to 2 ml of plasma, the plasma sample is deproteinized, extracted into butanol, back extracted into HCl, derivatized to the pentafluorobenzyl derivative (CH2C6F5)3-histamine, purified on silica gel columns, and then quantified with negative ion-chemical ionization mass spectrometry by selected ion monitoring of the ratio of ions m/z 430/434. For N tau-methylhistamine, after the addition of N tau-[2H3]methylhistamine to 2 ml of plasma, the plasma sample is deproteinized, extracted into butanol, back extracted into HCl, derivatized to the heptafluorobutyryl derivative (C3F7CO2)2-N tau-methylhistamine, purified on silica gel columns, and then quantified with negative ion-chemical ionization mass spectrometry by selected ion monitoring of the ratio of ions m/z 497/500. The precision of the histamine assay is 3.1% and the accuracy is 95.5 +/- 2.5% while the precision of the N tau-methylhistamine assay is 1.9% and the accuracy is 106.8 +/- 1.9%. The lower limits of sensitivity are 1 pg for histamine and 6 pg for N tau-methylhistamine injected on column. Using the assay in three normal human volunteers, plasma concentrations of histamine were 130, 92, and 85 pg/ml, and of N tau-methylhistamine were 229, 228, and 216 pg/ml. This assay provides a very sensitive and accurate method of quantitation of histamine and N tau-methylhistamine in plasma samples.     

Biomass Pyrolysis in an Argon/Hydrogen Plasma Reactor

This paper presents the experimental results of biomass pyrolysis in a laboratory argon/hydrogen plasma reactor. The samples tested were wood and rice husk. The gaseous product was found to contain mainly H₂, CO, C₂H₂ and CH₄. The conversion of carbon and oxygen from the biomass feed to gaseous product can reach up to 79 % and 72 %, respectively. The results indicate that plasma pyrolysis of biomass may be a useful way for gaseous fuel production.     

Carbonic anhydrase activity of rabbit lungs

Pulmonary carbonic anhydrase (CA) activity was studied in rabbit lungs perfused with solutions containing no CA. Measurements were made of the amount of 14CO2 appearing in the expired gas following injections of H14CO3(-), 14CO2, or a 20:1 mixture of each into the pulmonary artery. The fraction of the injected label in the expired gas was only 17% greater for 14CO2 than for the mixture, suggesting that equilibration between H14CO3(-) and 14CO2 was nearly complete during the capillary transit time. Inhibition of pulmonary CA decreased excretion of H14CO3(-) and the mixture by 40 and 49% and increased the excretion of 14CO2 by 96%. Addition of CA to the perfusate had no effect. Thus, CO2 exchange is not significantly limited by pulmonary CA if inhibitors are absent. Tissue binding of [3H]acetazolamide injected into the pulmonary artery was diminished by 50% when acetazolamide concentrations reached 0.13 x 10(-6) M. Each liter of extravascular lung water contained 1.25 x 10(-6) mol of receptors for acetazolamide that were accessible to plasma during a single circulation. Binding of [3H]acetazolamide was also observed in lungs of anesthetized rabbits, suggesting that pulmonary CA is accessible to plasma in vivo as well as in situ.     

Boron-containing folate receptor-targeted liposomes as potential delivery agents for neutron capture therapy

Boron neutron capture therapy (BNCT) depends on the selective delivery of a sufficient number of (10)B atoms to tumor cells to sustain a lethal (10)B(n,alpha)(7)Li reaction. Expression of FR frequently is amplified among human tumors. The goal of the present study was to investigate folate receptor (FR)-targeted liposomes as potential carriers for a series of boron-containing agents. Two highly ionized boron compounds, Na(2)[B(12)H(11)SH] and Na(3) (B(20)H(17)NH(3)), were incorporated into liposomes by passive loading with encapsulation efficiencies of 6% and 15%, respectively. In addition, five weakly basic boronated polyamines were investigated. Two were the spermidine derivatives: N(5)-(4-carboranylbutyl)spermidine.3HCl (SPD-5), N(5)-[4-(2-aminoethyl-o-carboranyl)butyl]spermidine.4HCl (ASPD-5). Three were the spermine derivatives: N(5)-(4-carboranylbutyl)spermine.4HCl (SPM-5), N(5)-[4-(2-aminoethyl-o-carboranyl)butyl]spermine.5HCl (ASPM-5), and N(5),N(10)-bis(4-carboranylbutyl)spermine.4 HCl (SPM-5,10). These were incorporated into liposomes by a pH-gradient-driven remote-loading method with varying loading efficiencies, which were influenced by the specific trapping agent and the structure of the boron compound. Greater loading efficiencies were obtained with lower molecular weight boron derivatives, using ammonium sulfate as the trapping agent, compared to those obtained with sodium citrate. The in vitro uptake of folate-derivatized, boronated liposomes was investigated using human KB squamous epithelial cancer cells, which have amplified FR expression. Higher cellular boron uptake (up to 1584 microg per 10(9) cells) was observed with FR-targeted liposomes than with nontargeted control liposomes (up to 154 microg per 10(9) cells), irrespective of the chemical form of the boron and the method used for liposomal preparation. KB cell binding of the FR-targeted liposomes was saturable and could be blocked by 1 mM free folic acid. Our findings suggest that further evaluation of FR-targeted liposomes is warranted to assess their potential as boron carriers for neutron capture therapy.     

Involvement of NADPH-dependent and cAMP-PKA sensitive H+ channels in the chorda tympani nerve responses to strong acids

To investigate if chorda tympani (CT) taste nerve responses to strong (HCl) and weak (CO(2) and acetic acid) acidic stimuli are dependent upon NADPH oxidase-linked and cAMP-sensitive proton conductances in taste cell membranes, CT responses were monitored in rats, wild-type (WT) mice, and gp91(phox) knockout (KO) mice in the absence and presence of blockers (Zn(2+) and diethyl pyrocarbonate [DEPC]) or activators (8-(4-chlorophenylthio)-cAMP; 8-CPT-cAMP) of proton channels and activators of the NADPH oxidase enzyme (phorbol 12-myristate 13-acetate [PMA], H(2)O(2), and nitrazepam). Zn(2+) and DEPC inhibited and 8-CPT-cAMP, PMA, H(2)O(2), and nitrazepam enhanced the tonic CT responses to HCl without altering responses to CO(2) and acetic acid. In KO mice, the tonic HCl CT response was reduced by 64% relative to WT mice. The residual CT response was insensitive to H(2)O(2) but was blocked by Zn(2+). Its magnitude was further enhanced by 8-CPT-cAMP treatment, and the enhancement was blocked by 8-CPT-adenosine-3'-5'-cyclic monophospho-rothioate, a protein kinase A (PKA) inhibitor. Under voltage-clamp conditions, before cAMP treatment, rat tonic HCl CT responses demonstrated voltage-dependence only at ±90 mV, suggesting the presence of H(+) channels with voltage-dependent conductances. After cAMP treatment, the tonic HCl CT response had a quasi-linear dependence on voltage, suggesting that the cAMP-dependent part of the HCl CT response has a quasi-linear voltage dependence between +60 and -60 mV, only becoming sigmoidal when approaching +90 and -90 mV. The results suggest that CT responses to HCl involve 2 proton entry pathways, an NADPH oxidase-dependent proton channel, and a cAMP-PKA sensitive proton channel.     

Assessment of the impact of excessive chemical additions to municipal wastewaters and comparison of three technologies in the removal performance of pathogens and toxicity

The removal efficiencies of pathogens such as Salmonella (S), helminths ova (H), protozoan cysts (P), total coliforms (TC), faecal coliforms (FC) and faecal streptococci (FS) by three treatment processes: aerated lagoon (AL), activated sludge (AS) and anaerobic membrane bioreactor (MBR) were evaluated by means of standard microbiological numeration methods. The micro-toxicity and phyto-toxicity of wastewaters were monitored by LUMIStox and germination index (GI) of Lepidium sativum tests. The results of municipal wastewaters receiving industrial effluents such as Sfax and Mahres were compared with other municipal wastewaters receiving mainly domestic effluents such as Ksour-Essaf. The anaerobic MBR allowed an effective removal of 100% for all the microorganisms tested. The average removal of TC, FC, FS, S, H and P was 1.65log(10), 1.42log(10), 1.23log(10), 0.91log(10), 52.23% and 76.15% in AL system and 0.62-0.84log(10), 0.87-0.93log(10), 0.71-0.78log(10), 0.81-2.71log(10), 59-74.1% and 59.84-72.2% in AS processes, respectively. LUMIStox and GI of L. sativum tests demonstrated that Ksour-Essaf wastewater (KW) was fairly toxic, while Sfax wastewater (SW) exhibited a high toxicity. This toxicity caused the inhibition of the anaerobic consortia when the MBR was fed with the SW. Moreover, the COD and the micro-toxicity increased during the day, parallel to the industrial and domestic activities resulting in the toxic character of SW during the day. SW treated in the AL remained toxic whereas the toxicity of KW treated in the AS or in anaerobic MBR decreased considerably. However, the anaerobic MBR showed a high efficiency in removing toxicity for both SW and KW. The quality of the anaerobic MBR permeate largely conforms with the microbiological WHO guidelines for unrestricted irrigation.     

Factors affecting the 16 alpha-hydroxylation of estrone 3-sulfate by guinea pig liver microsomes

The estrone 3-sulfate 16 alpha-hydroxylase of guinea pig liver microsomes has been demonstrated to be sensitive to CO. A CO/O2 ratio of 0.64 caused 50% inhibition of activity. Since inhibition was also obtained in the presence of 2-diethylaminoethyl-2,2-diphenylvalerate . HCl it seems likely that the hydroxylase is a cytochrome P450 containing system. A fourfold increase in enzyme activity was brought about by 40 mM Mg2+ or Ca2+ while the same concentration of Mn2+ resulted in a twofold increase. Lesser increases were seen with Na+ or K+ and complete inhibition was obtained in the presence of Fe2+, Cu2+, or EDTA. When assayed in the presence of detergent concentrations sufficiently small to guard against cytochrome P450 destruction, it was found that Cutscum, Triton X-100, and Triton N-101 each caused greatest inhibition of enzyme activity. Lesser inhibition was apparent in the presence of Miranol H2M, cholate, or deoxycholate. The nonionic detergent, Brij 35, caused least inhibition of all and, when hepatic microsomes were treated higher concentrations of Brij 35, about 80% of protein and over 95% cytochrome P450 were to be found in the 100 000 X g supernatant. Microsomal activity was more stable when stored at -20 degrees C in buffer containing glycerol, EDTA, and dithiothreitol than in buffer alone. Under best conditions only 10% of the hydroxylase activity was lost in one week.     

Fast stopped-flow microcalorimeter

A fast stopped-flow microcalorimeter using a thermistor and an a.c. bridge is described. Time resolution, limited by the response of the thermistor, is 3 ms for t 1/2 while sensitivity is 100 mu degree C in this bandpass. A reaction requires 0.3 ml of each reactant. The microcalorimeter is adiabatic to within 2% for 2 s and mixing may be repeated every 5 min. Computer finite element simulation techniques (FEST) are used to correct for the thermistor response time and heat losses. Results of tests with reactions of NaOH and HCl, NaHCO3, and HCl, and glyclyglycine and CO2 agree with published kinetic and thermodynamic values to within an experimental error of less than 2%.     

Extracellular acidification at the surface of depolarized voltage-clamped snail neurones detected with eccentric combination pH microelectrodes

A new design of double micropipette was used to measure intracellular pH, membrane potential, and surface pH of superfused snail neurones. A third double micropipette was used to control the membrane potential via a CsCl-filled barrel and inject HCl iontophoretically. In one series of experiments the surface pH fell by up to one-third of a pH unit when the membrane potential was clamped to 20 mV, pHi was initially 6.7, and extracellular pH was about 7.4 in a medium buffered either with 2 mM HEPES or 2.7% CO2 and 20 mM bicarbonate. In a second series in which surface pH was observed during brief depolarizations to different potentials with different pHi, the potential at which the surface began to acidify varied with pHi with a slope of 32 mV per pH unit. The results confirm that H+ ions leave depolarized snail neurones if the electrochemical gradient is favourable and show that CO2-bicarbonate buffered solutions have a low effective extracellular buffering power for rapid additions of acid.     

Photodissimilation of Fructose to H(inf2) and CO(inf2) by a Dinitrogen-Fixing Cyanobacterium, Anabaena variabilis

The ability of cyanobacteria to serve as biocatalysts in the production of H(inf2) as a fuel and chemical feedstock was investigated with Anabaena variabilis. The results show that A. variabilis, when incubated under argon, dissimilated fructose to H(inf2) and CO(inf2) in a light-dependent reaction. The H(inf2) production had an obligate requirement for fructose and was heterocyst dependent, since NH(inf4)(sup+)-grown cultures lacking heterocysts failed to produce H(inf2). Differential inhibition studies with CO showed that nitrogenase is the main enzyme catalyzing the H(inf2) production. Net H(inf2) yield increased with increasing concentrations of fructose up to 10 mM in the medium. The average apparent conversion efficiency of fructose to H(inf2) (net H(inf2) produced/fructose removed from the medium) was about 10, although higher conversion efficiencies of 15 to 17 could be obtained during shorter periods and at optimum fructose concentrations. Under the same conditions, the ratio of CO(inf2) released to fructose removed from the medium was about 3.5, suggesting that only a fraction of the fructose carbon was completely oxidized to CO(inf2). Under conditions of carbon excess, which prevents H(inf2) uptake, the maximum ratio of H(inf2) to CO(inf2) was found to be 3.0. This is higher than the expected value of 2.0, indicating that water was also a source of reductant in this fructose-mediated H(inf2) production. Inhibition of H(inf2) evolution by 3-(3,4-dichlorophenyl)-1,1-dimethylurea confirmed a role for photosystem II in this process. The rate of H(inf2) production by A. variabilis SA1 was 46 ml h(sup-1) g (dry weight)(sup-1). This high rate was maintained for over 15 days. About 30% of this H(inf2) was derived from water (10 ml of H(inf2) h(sup-1) g [dry weight](sup-1)). These results show that filamentous, heterocystous cyanobacteria can serve as biocatalysts in the high-efficiency conversion of biomass-derived sugars to H(inf2) as a fuel source while simultaneously dissimilating water to H(inf2).     

Characterization of products from the pyrolysis of rapeseed oil cake

The main aim of this study was to investigate the composition of products from the pyrolysis of rapeseed oil cake in a fixed bed reactor at 400, 450, 500, 700 and 900 degrees C. The gas products mainly consisted of CO(2), CO, CH(4) and H(2)S at 500 degrees C. Empirical formula of bio-oil from the pyrolysis of rapeseed oil cake was CH(1.59)O(0.16)N(0.116)S(0.003) for 500 degrees C. Bio-oils mainly contained oleic acid, 1H-indole, 2,3,5-trimethoxy toluene, toluene, (Z)-9-octadecanamide, psoralene, phenol and phenol derivatives at all pyrolysis temperatures. Both non-aromatic and aromatic hydrocarbon compounds were determined in water phase of liquid product by Headspace-GC analysis. The heating values of bio-chars were found to be similar (24MJkg(-1)) at all pyrolysis temperatures.