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An Apparatus for Measurement of Carbonate

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TL;DR

This study presents a simple apparatus for carbonate measurement that uses hydrochloric acid to release CO2 from carbonates in a sealed reactor, with detection via thermal conductivity. Under optimal conditions, it provides accurate, reproducible results within 10 minutes, notably for sodium carbonate in heavy-duty detergents.

Abstract
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A simple apparatus for the determination of carbonate is developed. Carbon dioxide is liberated from carbonates by hydrochloric acid in a sealed glass reactor. Head space gas in the reactor containing air and carbon dioxide is directly introduced into separating column with 4-way cock, and detected with thermal conductivity detector. Digital integrator is used for measuring the peak area of carbon dioxide.Volume of the reactor cell, inject-time (which is the most important factor for determining carbon dioxide in this apparatus.) and some other operating conditions are discussed. Thus, under the optimum conditions, accurate and reproducible data were obtained more rapidly (within 10 minutes) in comparison with other conventional methods.This technique is particularly applicable to the determination of sodium carbonate in heavy duty detergents.

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  • Dec 1, 2006
  • Washington Tru Solutions Llc, Hanford, Wa (United States)

This document describes and implements the process to establish the concentration of flammable gas/volatile organic compounds (VOCs), hydrogen, and methane in a waste container intended for shipment in the Transuranic Package Transporter-II (TRUPACT-II) or HalfPACT packagings. An aliquot of headspace gas (HSG) is sampled from a waste container and analyzed using one analytical unit which is a gas chromatograph (GC) with two detectors, a mass spectrometer (MS) and a thermal conductivity detector (TCD). The sample introduced to the GC is split and part goes to MS and the other part goes to TCD. The MS analyzes sample for volatile organic compounds (VOC) and the TCD analyzes for hydrogen and methane. The requirements and technical bases for allowable flammable gas/VOC concentrations are described in the Contact-Handled Transuranic Waste Authorized Methods for Payload Control (CH-TRAMPAC).

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  • Mar 1, 2007
  • Washington Tru Solutions Llc, Hanford, Wa (United States)

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  • Washington Tru Solutions Llc, Hanford, Wa (United States)

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  • Research Article
  • 10.1149/ma2019-02/22/1069
Electrochemical Reduction of Carbon Dioxide on Lanthanum Based Transition Metal Oxide Electrocatalysts
  • Sep 1, 2019
  • Electrochemical Society Meeting Abstracts
  • Madhurima Barman + 2 more

Among the various methods available for reduction of CO2, the electrochemical reduction method stands out due to it being capable of producing industrially important fuels, organic chemicals and pure oxygen. Such process takes place in an electrochemical cell, where carbon dioxide is reduced to at room temperature and atmospheric pressure, using only water, carbon dioxide and electricity at specific electrochemical potentials. Here, electrocatalysts have an important role to play, for enhancing the kinetics of the process and also for rendering the formation of desired products feasible at some selected potentials. In the present research, we are exploring the usage of La-based transition metal (TM) oxides, crystallizing in perovskite structure, as electrocatalysts. The synthesis of these metal oxides is cost effective and tuning the performance via doping is facile. Furthermore, these perovskites are stable in stoichiometric, as well as non-stoichiometric, forms and due to the basicity of La exhibits affinity for CO2. Accordingly, here we have investigated the efficiency and effectiveness of different La-based TM oxides, as electrocatalysts, towards the formation of industrially relevant products upon reduction of CO2. It may be mentioned here that, in order to enhance the efficiency of the electrocatalysts, as well as the mass transport of CO2 to the surface of the electrocatalysts, we have designed a new electrolysis cell where gas diffusion electrode (GDE) containing the electrocatalysts is used as working electrode. All the La-based TM oxides (i.e., LaCoO3, LaCrO3, LaFeO3, LaMnO3, LaNiO3) were synthesized via citrate solution-combustion route and calcined in air atmosphere at 850 oC for 6 h, with the heating rate being 10 oC/minute. Phase evolution of the TM oxides before and after usage, as electrocatalysts, were checked using X-ray diffraction (XRD; EMPYREAN PANalytical diffractometer) having Cu Kα radiation and scanning at a rate of 1 o/min between 10 to 90o. Inorganic Crystal Structure Database was used for the phase analysis of the powder catalysts. The composition of the perovskite catalysts (in terms of the ratios of the metals) were quantitatively analyzed by energy dispersive spectroscopy (EDS; QUANTA 200). Morphologies of the oxide particles were observed using scanning electron microscopy (SEM) JEOL JSM-7600F. The specific surface area of the perovskite catalysts were measured via BET using Micromeritics 3 FLEX Surface Characterization. The electrochemical CO2 reduction reaction was performed in an electrolysis cell via chronoamperometry using Biologic potentiostat (Model VSP 300). The reduction reactions were carried out on gas diffusion electrode (GDE) using basic aqueous electrolyte. The applied potentials were -1.1 V, -1.3 V, -1.5 V, -1.7 V, -1.9 V and -2.1 V vs. Hg/HgO, as reference electrode. The chronoamperometry experiments were performed for 3 h at each potential. The current densities obtained during the electrochemical CO2 reduction experiments were obtained for all the La-based TM oxide electrocatalysts used, viz., LaCoO3, LaCrO3, LaFeO3, LaMnO3, LaNiO3. The liquid products present in the electrolyte after the experiments were analyzed by high performance liquid chromatography (HPLC) using Agilent 1260 infinity series model with Aminex HPX-87H column. The gaseous products were analyzed by gas chromatography - thermal conductivity detector (GC-TCD) using Nucon 5700 gas chromatography. XRD scans recorded with the as-synthesized and calcined La-based TM oxides indicate that the oxides were phase pure (as shown in Fig. 1). The crystal structure was established as perovskite. The composition of the as-synthesized and calcined perovskite electrocatalysts, as determined using EDS, were in good agreement with the target compositions. The current densities were fairly stable during the 3 h long experiments for all the potentials studied; with an example being shown in Fig. 2. All the electrocatalysts produced formate (HCOO-), acetate (CH3COO-) and hydrogen as the products of electrochemical CO2 reduction. Furthermore, ethanol (C2H5OH) and 1-propanol (C3H7OH) were also formed on LaCoO3, with LaMnO3 being able to produce 1-propanol (C3H7OH) as one of the products. Hence, as per the present set of results in the context of the formation of desired products, LaCoO3 and LaMnO3 seem to be more promising among the La-TM-oxide electrocatalysts studied here. Keywords: CO2 reduction, transition metal oxide, electrocatalyst, chronoamperometry, reaction product. Figure 1

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