ライフサイエンスコーパス: pyrolysis

1 llowed by adsorption of furfuryl alcohol and pyrolysis.

2 l and thus to be accessible via flash vacuum pyrolysis.

3 housand,) with that of the CH3Cl released on pyrolysis.

4 e development of catalysts in catalytic fast pyrolysis.

5 a novel synthetic route based on flame spray pyrolysis.

6 tions, and energy balances from biomass slow pyrolysis.

7 anted in it by PANI/mesoporous silica during pyrolysis.

8 ketones were detected especially in acetone pyrolysis.

9 atic hydrocarbons were formed during partial pyrolysis.

10 synthesised from sodium alginate via furnace pyrolysis.

11 rete Sb-SnO2 islands, were prepared by spray pyrolysis.

12 ime by ultrasonic atomization-assisted spray pyrolysis.

13 completely overcome after 10 min of reactive pyrolysis.

14 Dimethyl ether pyrolysis (2% CH3OCH3/Ar) was observed behind the reflec

15 mass and after combustion (250 degrees C) or pyrolysis (400 degrees C).

16 Post-pyrolysis air oxidation (PPAO) at 400 degrees C of anoxi

17 ns were determined applying 800 degrees C of pyrolysis and 1800 degrees C of atomization temperatures

18 The method was optimized by building up pyrolysis and atomization curves in sample medium and by

19 simulate thermochemical conversion via fast pyrolysis and catalytic upgrading of bio-oil to renewabl

20 ly, N-CDs were prepared from L-asparagine by pyrolysis and characterized by different spectroscopic a

21 ion) and haloketone formation (increased for pyrolysis and decreased for oxidation).

22 Total PAH concentrations in the fast pyrolysis and gasification biochar were 0.3 mug g(-1) an

23 nt and speciation in biochars generated from pyrolysis and gasification of oak and corn stover were d

24 stion, whereas SO(3) was undetectable during pyrolysis and gasification.

25 roduced using the industrial methods of fast pyrolysis and gasification.

26 or haloacetonitrile formation (unchanged for pyrolysis and increased for oxidation) and haloketone fo

27 ng a thermal separation probe to perform the pyrolysis and sample introduction.

28 d chitosan-ruthenium-silica mesophase before pyrolysis and silica removal.

29 ciation in chars derived from thermal (i.e., pyrolysis) and hydrothermal treatments of municipal sewa

30 unburned and burned detritus under hypoxic (pyrolysis) and oxic conditions (thermal oxidation) at 25

31 ssions, food production and industries, coal pyrolysis, and various biological activities).

32 tensity (CI) to more accurately characterize pyrolysis, and we document variation in charcoal chemica

33 s to levoglucosan (LGA)-the major product of pyrolysis-and also to minor products such as 5-hydroxy-m

34 and structure-controllable ultrasonic spray pyrolysis approach using energetic carbon precursors.

35 Metal-nitrogen-carbon materials prepared via pyrolysis are promising single-atom catalysts but often

36 features down to 200 mum are obtained after pyrolysis at 1000 degrees C in a nitrogen atmosphere.

37 Pyrolysis at 180 degrees C leads to a CNP molecular prec

38 and short-chain polyphosphates formed after pyrolysis at 250-600 degrees C.

39 nascent decomposition processes in cellulose pyrolysis at 327 and 600 degrees C using Car-Parrinello

40 mers at 250-350 degrees C in air followed by pyrolysis at 850 degrees C in an N(2) atmosphere.

41 ; uncertainties represent 1 SD), mainly coal pyrolysis at low temperature ( approximately 650 degrees

42 The effects of sample amount, pyrolysis/atomization temperatures on the determination

43 he greenhouse gas (GHG) balance of a modeled pyrolysis based biochar system via the computation of gl

44 te and separate high-value alkylphenols from pyrolysis bio-oil, produced directly from lignocellulosi

45 By applying this procedure to pyrolysis bio-oil, the primary products (phenol/4-alkylp

46 Except for the fast-pyrolysis biochar, KBC greatly exceeded the soil organic

47 .07 mug g(-1) to 3.27 mug g(-1) for the slow pyrolysis biochars and were dependent on biomass source,

48 but much shorter heating durations than slow-pyrolysis biochars, resulting in differing physicochemic

49 These slow pyrolysis biochars, which can be produced locally on far

50 rbon sequestration potentials than most slow-pyrolysis biochars.

51 Additionally, typical literature known pyrolysis biomass marker were confirmed by their element

52 chanisms (Maillard reaction, caramelisation, pyrolysis) by which they were formed.

53 (the carbon-rich solid formed during biomass pyrolysis) can provide carbon-negative bioenergy if the

54 Here, a ramped pyrolysis carbon isotope technique is employed to invest

55 n comparing the different use options of the pyrolysis char, the most favorable result is obtained fo

56 Pyrolysis combustion flow calorimetry reveals that these

57 g biomass conversion technologies (microwave pyrolysis, combustion, wet lipid extraction, and hydroth

58 rder of magnitude higher for low temperature pyrolysis compared to high temperature combustion.

59 from different feedstock and over a range of pyrolysis conditions are redox-active and reversibly acc

60 Biochars produced under pyrolysis conditions at 500-600 degrees C contain sulfat

61 x properties of chars formed under different pyrolysis conditions has been performed.

62 markers for specific feedstock materials and pyrolysis conditions of biochars in environmental system

63 Smoke was generated under pyrolysis conditions that simulated bushfire temperature

64 ns, implying considerable latitude to choose pyrolysis conditions to optimize for desired biochar pro

65 tion temperature is often used as a gauge of pyrolysis conditions, pyrolysis duration also changes ch

66 arrier accessible under typical flash vacuum pyrolysis conditions.

67 ood on glowing embers, that is, slow burning pyrolysis conditions.

68 and wood) under wildfire charring- and slow-pyrolysis conditions.

69 marily when the enzyme is activated prior to pyrolysis, consistent with increased lignin degradation

70 However bio-oil from fast pyrolysis contains a large amount of oxygen, distributed

71 ded quantitatively either under flash vacuum pyrolysis, conventional heating, or microwave irradiatio

72 High-temperature pyrolysis conversion of organic analytes to H(2) in hydr

73 Overall, these results suggest that soil pyrolysis could be a viable thermal treatment to quickly

74 IS) for lignin quantification via analytical pyrolysis coupled to gas chromatography with mass-spectr

75 Pyrolysis coupled to gas chromatography/mass spectrometr

76 fingerprint of the colloids was obtained by pyrolysis coupled with gas chromatography-mass spectrome

77 carbon isotope signature generated by online pyrolysis (delta(13)C(pyr)) showed little variation (+/-

78 sotope signature of AEOs generated by online pyrolysis (delta(13)Cpyr), natural abundance radiocarbon

79 I and GHG emissions (gCO2e/MJ-fuel) for fast pyrolysis derived fuels range from 1.52 to 2.56 and 22.5

80 formance and GHG reduction potential of fast pyrolysis-derived fuels are highly sensitive to the choi

81 Oxidative pyrolysis did not result in large differences from pyrol

82 ten used as a gauge of pyrolysis conditions, pyrolysis duration also changes charcoal physicochemical

83 etene curcumin is formed as a consequence of pyrolysis during common household cooking, showing stron

84 ger sized mode dominating under slow burning pyrolysis (Dva approximately 600 nm).

85 al (e.g., Stober silica) or high-temperature pyrolysis (e.g., fumed silica) routes.

86 forded 3-styrylindazole 58, which on further pyrolysis eliminated N2 to generate 3- and 2-phenylinden

87 lculations provided essential information on pyrolysis energy barriers and the involved reaction mech

88 Via flash vacuum pyrolysis, even metaparacyclophanes as small and straine

89 explored to provide a theoretical account of pyrolysis experiments by Huntsman, Baldwin, and Roth on

90 The high-T/p liquid-phase "flash flow pyrolysis" (FFP) technique was applied to the thermolysi

91 were used to determine the rate constants of pyrolysis for H4S from 300 to 1000 K.

92 Although the different steps (extraction and pyrolysis) fractionate between (12)C and (13)C, the isot

93 s of 44 using the falling solid flash vacuum pyrolysis (FS-FVP) method afforded cyclopenta[def]phenan

94 drazone using the falling solid flash vacuum pyrolysis (FS-FVP) method.

95 were generated by falling solid flash vacuum pyrolysis (FS-FVP).

96 cm(-1) by a combination of mild flash vacuum pyrolysis (FVP) at 200-600 degrees C with low temperatur

97 Flash vacuum pyrolysis (FVP) is a gas-phase continuous-flow technique

98 Flash vacuum pyrolysis (FVP) of 1-(5-(13)C-5-tetrazolyl)isoquinoline

99 Flash vacuum pyrolysis (FVP) of azides is an extremely valuable metho

100 1,5-a]quinoline by conventional flash vacuum pyrolysis (FVP) were observed by IR spectroscopy.

101 luable soil amendment as well as bio-oil and pyrolysis gas (py-gas) that can be used for energy.

102 Pyrolysis gas chromatography/mass spectrometry (Py-GC-MS

103 A novel analytical approach based on pyrolysis-gas chromatography coupled with mass spectrome

104 In this study Curie-Point pyrolysis-gas chromatography-mass spectrometry combined

105 Samples were analyzed using pyrolysis-gas chromatography-mass spectrometry with in s

106 y chemical characterisation using whole-rock pyrolysis-gas chromatography-mass spectrometry.

107 was analysed using elemental analysis (EA), pyrolysis-gas chromatography/flame ionisation detection

108 aphy/flame ionisation detection (Py-GC/FID), pyrolysis-gas chromatography/mass spectrometry (Py-GC/MS

109 at affected lignin chemistry on the basis of pyrolysis-gas chromatography/mass spectrometry analysis.

110 zation was performed by CLSM, AFM, ATR-FTIR, pyrolysis GC-MS, and ICP-MS techniques.

111 Laser microscope dissection/pyrolysis GC/MS, histochemical staining/lignin analyses,

112 Pyrolysis-GC-MS analysis showed more reduction in the le

113 state-of-the-art methods, such as TGA-MS and pyrolysis-GC.

114 By using a novel quantitative pyrolysis-GC/MS analysis for rubber polymer, we detected

115 Pyrolysis-GC/MS and 2D-NMR analysis of P. radiata TE cul

116 ds were identified in TEs by thioacidolysis, pyrolysis-GC/MS and/or 2D-NMR in CCR-RNAi lines, providi

117 into transportation fuels via catalytic fast pyrolysis has attracted much attention.

118 mistry of products formation in hydrocarbons pyrolysis has been explored via a comparative experiment

119 iate that was generated by high-vacuum flash pyrolysis (HVFP) of the corresponding p-tosylhydrazone s

120 ning chemical components into SO2 by thermal pyrolysis in a high temperature furnace at atmospheric p

121 e)4 with ammonia followed by low-temperature pyrolysis in ammonia.

122 and post exposure bake settings followed by pyrolysis in an inert environment.

123 Wastewater biosolids pyrolysis is a promising technology that could help faci

124 Carbon pyrolysis is a widespread method for synthesizing carbon

125 n of bio-oil recovered from corn stover fast pyrolysis is blended and co-fired with bituminous coal t

126 omposed of uranium oxide using aerosol spray pyrolysis is characterized with respect to the various p

127 lowing: (a) product formation in hydrocarbon pyrolysis is dominated by hydrogen abstraction and a vin

128 Here, rapid pyrolysis is integrated with direct analysis in real tim

129 t carbohydrate product of cellulosic biomass pyrolysis is the anhydrosugar levoglucosan (1,6-anhydro-

130 otein synthesis (MPS) via gas chromatography-pyrolysis-isotope ratio mass spectrometry.

131 mporally quantify MPS via gas chromatography:pyrolysis:isotope ratio mass spectrometer.

132 rocarbons (PAHs) was not observed, with post-pyrolysis levels well below applicable standards.

133 ectrometry (FT-ICR-MS) for the analysis of a pyrolysis liquid from brown coal.

134 Pyrolysis liquids from coal are complex mixtures of orga

135 regarding high-molecular-weight compounds in pyrolysis liquids, although their characterization is im

136 tional liquid chromatography-based analyses, pyrolysis mass spectrometry achieved at least 250-fold h

137 dification, thermal drying, incineration and pyrolysis may decrease NH3 (9-11%) and GHG (11-18%) emis

138 gn a gradient electrospinning and controlled pyrolysis method to synthesize various controllable 1D n

139 article were synthesized using a flame spray pyrolysis method.

140 our composition gradient electrospinning and pyrolysis methodology may lead to further developments i

141 Pyrolysis molecular beam mass spectrometry was used to d

142 ant inbred maize (Zea mays) population using pyrolysis molecular-beam mass spectrometry to establish

143 Flash vacuum pyrolysis of 1,3-bis-iodomethyl-benzene (m-C8H8I2) produ

144 Similar pyrolysis of 2-phenyl-5-styryltetrazole 43 afforded 3-st

145 Flash vacuum pyrolysis of 44 using the falling solid flash vacuum pyr

146 Pyrolysis of 6,6-diacetoxy-2-methyl-2,4-cyclohexadienone

147 g a scalable, one-step process involving the pyrolysis of a polyaniline aerogel synthesized in the pr

148 The solution-based pyrolysis of a series of heterobimetallic Schiff base co

149 Laser power is sufficient to induce pyrolysis of a suitable substrate with the deposited sam

150 orks codoped with nitrogen and phosphorus by pyrolysis of a supermolecular aggregate of self-assemble

151 pectrometry technique, gas-phase products of pyrolysis of acetylene (ethyne, C(2)H(2)), ethylene (eth

152 arbon ring microelectrodes were deposited by pyrolysis of acetylene in the lumen of these quartz capi

153 was generated in high yields by flash vacuum pyrolysis of allyl phenyl ether 2 with subsequent trappi

154 "PMCS") are successfully synthesized by the pyrolysis of an imidazolate framework using a mesoporous

155 Many studies related to catalytic fast pyrolysis of biomass have been published.

156 n the experimental studies on catalytic fast pyrolysis of biomass is also summarized with the emphasi

157 Fast pyrolysis of biomass is recognized as an efficient and f

158 manipulation of the primary products of fast pyrolysis of carbohydrates.

159 The method was then used to examine fast pyrolysis of cellobiose.

160 provide insights into the mechanisms of fast pyrolysis of cellulose.

161 and small molecules was predominant for the pyrolysis of cellulose.

162 Through flash vacuum pyrolysis of CF3 S(O)NCO at ca. 1200 K, sulfinyl isocyan

163 methyl sulfide (DMS), was generated by flash pyrolysis of CH3SO2OOSO2CH3 and subsequently isolated in

164 wise referred to as C-dots, by following the pyrolysis of citric acid (CA)-ethanolamine (EA) precurso

165 developed by using simple microwave assisted pyrolysis of citric acid and sodium thiosulphate.

166 s are synthesized through controlled thermal pyrolysis of citric acid and urea.

167 ere synthesized using the one-step microwave pyrolysis of citric acid in the presence of diethylenetr

168 d graphene layers on alumina are obtained by pyrolysis of Co(OAc)2/phenanthroline.

169 cobalt-based catalysts have been prepared by pyrolysis of cobalt complexes with nitrogen ligands on d

170 Pyrolysis of contaminated soils at 420 degrees C convert

171 degrees C) microwave-assisted (MW-assisted) pyrolysis of DIR allows for simultaneously efficient fas

172 ared by a facile and scalable method through pyrolysis of electrospun polyimide.

173 tensity of ions from the aerosol produced by pyrolysis of ethyl cellulose are observed in the mass sp

174 The products of the pyrolysis of four sesquiterpenes, beta-caryophyllene, al

175 e in high yields (up to 66%) by flash vacuum pyrolysis of FSO(2)N(3).

176 The pyrolysis of H4S was simulated with kinetic Monte Carlo

177 n a simple, scalable and two-step method via pyrolysis of iron acetate and phenanthroline and subsequ

178 rrent understanding of the chemistry in fast pyrolysis of lignocellulose and focuses on the developme

179 the characterization of aqueous phases from pyrolysis of lignocellulosic biomasses.

180 de (RDA/ICE) reaction under the flash-vacuum pyrolysis of maleic anhydride adducts is developed.

181 hether chloromethane (CH3Cl) detected during pyrolysis of Martian soils by the Viking and Curiosity M

182 duce stable molten metal alloy catalysts for pyrolysis of methane into hydrogen and carbon.

183 of 3D graphitic carbon networks through the pyrolysis of nanosized ZIF-67 crystals.

184 Pyrolysis of nitrogen-ligated cobalt(II) acetate support

185 errestrial environment CH3Cl released during pyrolysis of organic matter derives from the methoxyl po

186 own to 1.2 mum were fabricated by controlled pyrolysis of patterned photoresist.

187 oducing liquid transportation fuels via fast pyrolysis of perennial grasses: switchgrass and miscanth

188 % with a pore-mouth-modified catalyst in the pyrolysis of pine wood.

189 orous graphitic carbon for iodine loading by pyrolysis of polyaniline coated cellulose wiper.

190 ed by high-temperature (up to 900 degrees C) pyrolysis of polyimide precursor hollow-fiber membranes.

191 synthesis of layered SiCN-MoS2 structure via pyrolysis of polysilazane functionalized MoS2 flakes.

192 Exothermic pyrolysis of refuse, which is hypothesized to be initiat

193 elatively slow rate of heating and prolonged pyrolysis of resinites using this new methodology, combi

194 d oxidized nitrogen-bearing compounds during pyrolysis of scooped aeolian sediments and drilled sedim

195 The CO(2) cofeed impact on the pyrolysis of styrene butadiene rubber (SBR) was investig

196 Upon flash vacuum pyrolysis of sulfinyl azide CF3S(O)N3 at 350 degrees C,

197 as sample (10% v/v H2S) that was produced by pyrolysis of sulfur-rich kerogen.

198 ) during low temperature (150-400 degrees C) pyrolysis of the carbonaceous chondrite Murchison with c

199 y influenced by the vitrification during the pyrolysis of the galvanic sludge.

200 e taint compounds are primarily derived from pyrolysis of the lignin component of fuels.

201 Pyrolysis of the MOF-shell composites produces hollow ca

202 imethylsilylcyclobutylidene was generated by pyrolysis of the sodium salt of the tosylhydrazone deriv

203 O, and other trace gases were evolved during pyrolysis of two mudstone samples acquired by the Curios

204 rs of increasing electrical conductivity via pyrolysis of wood shavings at increasing temperature.

205 har is the product of incomplete combustion (pyrolysis) of organic material.

206 hemical conversion processes such as biomass pyrolysis or gasification as well as the synthesis of bi

207 be applied to various heterogenic combustion/pyrolysis or reaction model systems, such as fossil- or

208 Under flash vacuum pyrolysis or under microwave irradiation, 1-methyl- and

209 e furnace under three different atmospheres: pyrolysis, oxy-fuel combustion, and carbon dioxide gasif

210 O(2), and CS(2) are the major species during pyrolysis, oxy-fuel, and gasification.

211 Here, we investigate its pyrolysis pathways by selecting n-heptane-4-sulfonic aci

212 The majority of products from partial pyrolysis peaked between 300 and 500 degrees C, whereas

213 A fast-pyrolysis probe/tandem mass spectrometer combination was

214 ate and high temperature and a non-catalytic pyrolysis process are presented.

215 y nanojunction is synthesized using a simple pyrolysis process followed by a hydrothermal treatment.

216 out through a facile, one-step, solid-state pyrolysis process in an inert atmosphere.

217 A novel pyrolysis process using wastewater biosolids-derived bio

218 rm discotic liquid crystal phases during the pyrolysis process.

219 s using a two-step, diffusion-assisted spray pyrolysis process.

220 ke of crack cocaine contains cocaine and its pyrolysis product, anhydroecgonine methyl ester (AEME).

221 lly increased the complete silylation of the pyrolysis products and the chromatographic resolution, r

222 For this purpose polymer characteristic pyrolysis products and their indicative fragment ions we

223 n increased fragmentation of ethyl cellulose pyrolysis products during ionization.

224 n was utilized to determine the initial fast-pyrolysis products for four different selectively (13)C-

225 tive response factors (RRFs) for the various pyrolysis products obtained were determined and applied.

226 ensitivity for the caffeine standard and the pyrolysis products of ethyl cellulose is maintained or i

227 The primary fast pyrolysis products were determined to consist of only a

228 Depending on the experiment, the pyrolysis products were either evaporated and quenched o

229 To determine the true primary pyrolysis products, a very fast heating pyroprobe was co

230 eaction and facilitate the derivatization of pyrolysis products, by enabling the materials to react w

231 e of the noncannabinoid plant components and pyrolysis products, followed by a discussion of 3 synthe

232 etection of molecular ions of combustion and pyrolysis products.

233 ther accounting for 62-96% of all quantified pyrolysis products.

234 solids played an important role in upgrading pyrolysis products.

235 r accounting for 3.9-44.5% of the quantified pyrolysis products.

236 ty of the ionization methods to ionize known pyrolysis products: glycolaldehyde, hydroxyacetone, furf

237 Ramped pyrolysis profiles indicate that the organic material wa

238 apidly through a very hot oven (flash vacuum pyrolysis) promotes high-temperature thermal reactions i

239 and 500 degrees C, whereas for conventional pyrolysis reaction products peaked between 400 and 500 d

240 A home-built flow tube that simulates pyrolysis reactor conditions was used to examine the sec

241 sonance was successfully interfaced with the pyrolysis reactor to elucidate the structures of the lab

242 to characterize the PAH evolution in modern pyrolysis reactors and assess the fate of biochar-bound

243 4 mmol H2 g(-1) plastic was obtained for the pyrolysis-reforming of HDPE waste in the presence of the

244 show that hydrogen can be produced from the pyrolysis-reforming process, but also carbon nanotubes a

245 from waste plastics is reported here using a pyrolysis-reforming technology comprising a two-stage re

246 truction zones in the various combustion and pyrolysis regions of a cigarette during puffing.

247 Several series of polymer pyrolysis residues, similar to those produced by classic

248 amine into an as-drawn CNT fiber followed by pyrolysis results in a direct insulation-to-conduction t

249 ously reported high-temperature flash vacuum pyrolysis results where the interconversion of carbene a

250 Ramped pyrolysis (RP) targets distinct components of soil and s

251 pping of a biochar produced from corn stover pyrolysis shows individual sulfur-containing mineral par

252 arts, is not direct and generally involves a pyrolysis step to produce ionizable species.

253 to avoid losses of Cl, Br, and I during the pyrolysis step, with concomitant use of Pd as a permanen

254 r and/or tarry deposits generated during the pyrolysis step.

255 Flash vacuum pyrolysis studies of substituted 6-acetoxy-2,4-cyclohexa

256 ase microextraction (HS-SPME) with an online pyrolysis system coupled with isotope ratio mass spectro

257 In this paper, a slow pyrolysis system for generating heat and biochar from li

258 on a glass substrate with the chemical spray pyrolysis technique.

259 tmosphere, it is not known how variations in pyrolysis temperature and feedstock type affect concentr

260 By regulating the thermal-pyrolysis temperature and ratio of reactants, the maximu

261 genic carbon to a lesser extent with greater pyrolysis temperature due to lower charging and discharg

262 gth, 606.440nm in a graphite tube applying a pyrolysis temperature of 1000 degrees C and a molecule f

263 alladium+citric acid modifier and applying a pyrolysis temperature of 1000 degrees C and a volatilisa

264 After a pyrolysis temperature of 1100 degrees C, the pristine an

265 conditions were found to be 213.561nm with a pyrolysis temperature of 1300 degrees C, a volatilizatio

266 Under experimental conditions of pyrolysis temperature of 640 degrees C and atomization t

267 ly coated platforms at 606.440 nm applying a pyrolysis temperature of 700 degrees C and a molecule fo

268 ernary-doped carbon (HQDC-X, X refers to the pyrolysis temperature) can be fabricated by directly pyr

269 y changing the amount of carbon loading, the pyrolysis temperature, and the post-treatment procedure.

270 ochars and were dependent on biomass source, pyrolysis temperature, and time.

271 igher ionic strength and lower pH, and (iii) pyrolysis temperature-dependent: 500 < 700 << 300 degree

272 phate being less extractable with increasing pyrolysis temperature.

273 om corn stalk biochar produced at increasing pyrolysis temperatures (350-650 degrees C) and from the

274 ts degradation of the cellulosic fraction at pyrolysis temperatures of 250 degrees C, whereas at high

275 barriers of 74-82 kcal/mol, consistent with pyrolysis temperatures of 900 to 1100 degrees C.

276 ible applications include verifying declared pyrolysis temperatures of biochars and evaluating ecosys

277 way, and porosity of biochar are observed at pyrolysis temperatures ranging from 250 to 550 degrees C

278 uid-phase FFP (molecule-molecule collisions) pyrolysis temperatures was derived.

279 he molecular fluorophores predominate at low pyrolysis temperatures while the carbogenic core starts

280 In the presence of the clay, at lower pyrolysis temperatures, the biochar develops a higher po

281 sis did not result in large differences from pyrolysis; the main products still were syringol, guaiac

282 With increasing pyrolysis time and temperature, PAH concentrations gener

283 count of the use low-temperature MW-assisted pyrolysis to effect this change.

284 ination to form silica replicas or reductive pyrolysis to form electrically conductive carbon replica

285 1,2-azaborine, is generated by flash vacuum pyrolysis, trapped under cryogenic conditions, and studi

286 relevant for the mechanistic understanding, pyrolysis under flow conditions or in solution or the so

287 tain the cylindrical shape of bacteria after pyrolysis under high temperatures, while heteroatoms inc

288 confirmed in biochar produced by pilot plant pyrolysis units.

289 Low temperature pyrolysis upon fuel addition resulted in "tar-ball" type

290 molten salt synthesis with ultrasonic spray pyrolysis (USP) for the first time.

291 l assembly technique called ultrasonic spray pyrolysis (USP).

292 The divergence between pyrolysis vapors and biochar in the distribution of WSOC

293 An empirical model of biomass slow pyrolysis was developed and applied to several pathways

294 that the carbonaceous material produced via pyrolysis was dispersed in the form of a layer coating t

295 ve methods (sequential chemical degradation, pyrolysis) were applied to obtain detailed information a

296 sidues, similar to those produced by classic pyrolysis, were obtained.

297 sistant and caryophyllene least resistant to pyrolysis with cedrene and valencene occupying intermedi

298 of different P species in the pyrochars from pyrolysis, with both total P and polyphosphate being les

299 It was found that maximum pyrolysis yield was ca. 50% depending on the oxidation c

300 Pyrolysis yielded an abundance of fragment ions (e.g., 1