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84 protocols using gc 2014c

1

Photocatalytic Hydrogen Production

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The photocatalytic reaction was conducted on an all glass automatic on-line trace gas analysis system (Labsolar-6A) and SHIMAZU gas chromatograph (GC-2014C). The hydrogen generated in the reactor was automatically entered into the gas chromatograph for detection. Fifty milligrams of catalyst was placed in the reactor and a 100 mL aqueous solution containing 10 mL of lactic acid was poured into the reactor. The reactor temperature was kept at 278 K by a low temperature thermostatic bath. The light source is a 300 W Xe lamp (λ ≥ 350 nm).
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2

GC-MS Analysis of 1,2-Propanediol Yield from PLA

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The reactants identification was carried out by Shimadzu QP 2010 Plus gas chromatography-mass spectrometry (GC-MS) with an Rtx-5MS column (30.0 m × 0.25 mm × 0.25 μm). The oven temperature was held at 60 °C for 5 min, and ramped to 260 °C for another 5 min at 12 °C/min. The injector and detector temperature were set at 280 °C and 285 °C, respectively.
The content of 1,2-propanediol (mol/L) was determined by a gas chromatograph (GC, Shimazu GC-2014C, Shimazu, Kyoto, Japan) equipped with a flame ionization detector (FID) and WondaCap FFAP capillary column (30.0 m × 0.25 mm × 0.25 μm). The initial column temperature was 60 °C holding for 5 min, and ramped to 260 °C at a rate of 12 °C/min. Both the injector and the detector temperature were set at 280 °C. The quantification was analyzed by the standard curves of each standard substance, using dodecane as the internal standard. The yield (%) of 1,2-PDO in the reaction bulk was calculated as Equation (1).
Yield %=mim0 × 100%
where mi (g) is the mass quantity of 1,2-PDO and m0 (g) refers to the mass of the PLA material.
The conversion (%) of PLA feedstock was calculated as Equation (2).
Conversion %=m0mrm0 × 100%
where mr (g) is the mass quantity of residues and m0 (g) refers to the mass of the PLA material.
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3

Analytical Methods for Biofuel Precursors

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Hydrogen and organic acids were determined by gas chromatography (GC-2014C, Shimadzu, Kyoto, Japan), equipped with a thermal conductivity detector, as detailed in a previous study67 (link). The ratio of α-1,4/1,6 oligosaccharides was determined with the Amylose/Amylopectin Assay Kit (Megazyme, Wicklow, Ireland). Organic acids and glucose were analyzed by high-performance liquid chromatography with refractive index and ultraviolet detectors and a Bio-Rad Aminex HPX-87H column. The analysis was performed using 5 mM sulfuric acid as the mobile phase at 55 °C with a flow rate of 0.5 mL min−1. The total starch concentration was determined by the DNS method.
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4

Analyzing N2O Concentrations Using Headspace GC

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The concentration of N2O was measured using static headspace gas chromatography (Xu et al., 2005 (link)). The water in the vial was replaced with 5 mL of He to achieve headspace, agitated vigorously for 15 min, and stored in the dark to attain gas–liquid equilibrium. A gas chromatograph equipped with an electron capture detector (GC-2014C, Shimadzu, Tokyo, Japan) was used to measure the concentration of N2O (CG) in the headspace. The dissolved N2O concentration (CL) before gas replacement and the △N2O (i.e., the net increase in N2O) were calculated by the following equations (Lin et al., 2016 (link)):
where K0 is the equilibrium constant (Weiss and Price, 1980 (link)); R is the ideal gas constant; T is the temperature at equilibrium; VG and VL are the gas and liquid volumes after He replacement, respectively; and CN2Oeq is the N2O concentration in equilibrium with the atmospheric concentration calculated based on Weiss and Price (1980) (link).
N2O saturation was calculated as follows:
The estimated N2O flux through the water–air interface was calculated as follows:
where K denotes the gas change rate calculated based on the method of Borges (2004) (link).
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5

Photocatalytic Hydrogen Production

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The photocatalytic H2 production experiments were conducted in a 400 mL Pyrex quartz glass reactor at normal pressure and temperature. The photocatalyst (100 mg) was dispersed in 100 mL of 10% aqueous methanol solution (methanol acting as a sacrificial agent) using a magnetic stirrer. Then the reaction mixture was dispersed in an ultrasonic washing bath for 10 min. Before the irradiation by a 300 W Xe lamp (CRL-HXF300, China) as the sunlight source, the reactor was deaerated with nitrogen gas. During the photocatalytic reaction, the reactant solution was maintained at room temperature by using a Low-temperature cooling circulating pump (CEL-CR300, China), and magnetic stirring was continually maintained to keep the photocatalyst suspended in the aqueous methanol solution. The amount of H2 generated was tested using an online Shimadzu GC-2014C gas chromatograph (Shimadzu, Japan) equipped with an MS-5A column. The total reaction time for each sample was 5 h, and the H2 concentration was measured every hour.
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6

Lipid Extraction and Fatty Acid Analysis

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Total lipids were extracted from samples of freeze-dried powder using petroleum ether as solvent at 50 °C for 8 h. Analyses of fatty acid methyl esters (FAME) were performed according to the ISO,method 5509, and gas chromatography analyses of FAME were carried out using SHIMADZU GC-2014C apparatus. For each tissue and each stage of development, lipid analysis was performed in biological triplicate under a completely random experimental design. The significance of difference between main fatty acid compositions at different stages each year was tested by analysis of variance and multiple comparisons (Duncan’s new multiple range test).
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7

Photocatalytic CO2 Reduction on Leaf-like Membranes

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The photocatalytic CO2RR tests of the leaf-like membranes in the GMG mode were carried out in a home-made outer irradiation-type gas-flow cell connected to a closed gas-circulation system (Supplementary Fig. 34). The as-prepared membranes were sandwiched by two gas chambers (Supplementary Fig. 35). During the photocatalysis process, humidified high-pure CO2 (99.9999%) was cycled continuously in the whole system by a gas-recycle-pump with tunable flow rates, so that the CO2 and water molecules could continuously pass across the membranes. Before tests, the whole catalytic system was thoroughly degassed to remove the air by high-purity Ar (99.9999%) displacement. After 30 min of high-purity (99.9999%) CO2 circulation, the membranes were illuminated by a 300 W Xe-lamp (Beijing China Education Au-light Co., Ltd.) with a 420 nm long-pass filter. The water vapor carried liquid products (e.g., HCOOH) were collected by a cold trap and then quantified with NMR. The gas-phase products (e.g., H2) were quantified by an online gas chromatography (Shimadzu GC-2014C).
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8

Photocatalytic Hydrogen Evolution

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The photocatalytic water-splitting hydrogen evolution was reacted in a closed Pyrex glass system (Beijing Perfectlight Technology Co., Ltd., Labsolar-6A, Beijing, China). Generally, 50 mg of 1.0 wt% Pt-loaded composite photocatalyst was dispersed in a 100 mL 10% triethanolamine (TEOA) aqueous solution. A 300 W Xe lamp (Beijing Perfectlight Technology Co., Ltd., Labsolar-6A, Beijing, China) with the 420 nm cut-off filter was used as the light source and adjusted to 500 mW cm−1. The temperature was controlled as constant at 10 °C via a circulation cooling water method. The amount of hydrogen produced was determined by gas chromatography (Shimadzu GC-2014 C).
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9

Photocatalytic Hydrogen Production

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Photocatalytic H2 evolution was injected into a 250 ml of quartz reactor with a visible-light source irradiation. As a typical synthesis experiment, 0.1 g of photocatalyst with a certain Pt cocatalyst (1 wt%) was dispersed in a mixed solution of aqueous solution (90 ml) and methanol (10 ml). The amount of H2 evolution was measured in a gas chromatograph (GC-2014C Shimadzu Corp., N2 as carrier gas). The time interval of sampling was performed at 40 min during the water splitting process.
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10

Elemental and Thermochemical Analysis of Biomass

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The CHNS elemental analysis of the biomass feedstocks, biocrude oils, and hydrochar were conducted by an elemental analyzer (Elementar Vario ELIII, Hanau, Germany). The content of moisture, volatile matter, and ash were measured by an automatic industrial analyzer (YXGYFX 7705B, U-Therm, Changsha, China). The amount of fixed carbon was calculated by the subtraction method. Thermogravimetric analysis (TGA) of biomass feedstocks and hydrochars was performed by a thermogravimetric analyzer (SDTQ600, TA Instruments, Newcastle, WA, USA). The functional groups of biomass feedstocks, biocrude oils, and hydrochars were evaluated by Fourier transform infrared spectroscopy (FTIR, spectrum 400, PerkinElmer, Waltham, MA, USA).
The gas was collected by a 10 mL syringe and then characterized offline by a Shimadzu GC-2014C gas chromatographer (GC, Shimadzu Corp., Kyoto, Japan) equipped with a thermal conductivity detector (TCD). A standard gas mixture containing H2, CO, CH4, CO2, C2H4, and C2H6 was quantified to calibrate the proportion (vol.%) of gaseous fractions. The gas compositions (≥C3) were not observed or negligible in this study. All GC measurements were repeated to ensure reproducibility.
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