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Biogas

Biogas is a renewable energy source produced through the anaerobic digestion of organic matter, such as agricultural waste, animal manure, and municipal solid waste.
It is primarily composed of methane and carbon dioxide, and can be used as a fuel for heating, electricity generation, or transportation.
Biogas production offers a sustainable solution for waste management while simultaneously providing a clean energy alternative to fossil fuels.
The PubCompare.ai platform can help optimize biogas research by assisting in the identification of the most reliable protocols from the scientific literature, preprints, and patents, thereby enhanceing reproducibility and accuracy for biogas projects.

Most cited protocols related to «Biogas»

The integrated plant was modeled assuming a 1G raw material loading of 360,000 tons dry grain per year and a 2G raw material loading of 180,000 tons dry wheat straw per year. These raw material loadings correspond to an estimated annual ethanol production of 200,000 m3, assuming C6 fermentation only. In some of the simulated cases, C5 fermentation was also considered, which increased the annual ethanol production to approximately 230,000 m3. It was assumed that the plant was in operation 8000 h per year, and could be managed by 28 people. One 1G case and six integrated 1G + 2G cases were modeled. In the integrated cases, ethanol, DDGS, and biogas production from the C5 sugars were investigated, as well as biogas upgrading to vehicle fuel quality. A sensitivity analysis was also performed for the six integrated cases to assess variations in the biogas yield which increased the investigated configurations to another six supplementary cases.
An overview of the process is shown in Fig. 11, and further details are provided in Section “Case description” below.

Schematic overview of the 1G + 2G process and alternative configurations

Simulations were performed with the flow sheeting program Aspen Plus (version 8.2 from Aspen Technology Inc., Massachusetts, USA). Data for biomass components such as cellulose and lignin were retrieved from the National Renewable Energy Laboratory (NREL) database developed for biofuel components [28 ]. The NRTL-HOC property method was used for all units except in the heat and power production steam cycle, where STEAMNBS was used. The simulation models were further developments of previous work by Wingren et al. [29 (link), 30 (link)], Sassner and Zacchi [31 (link)] and Joelsson et al. [32 ]. Heat integration was implemented as described previously [32 ] using Aspen Energy Analyzer (version 8.2). The results from Aspen Plus were implemented in APEA, and were used together with vendors’ quotations to evaluate the capital and operational costs. Further details on the Aspen Plus modeling can be found in a previous publication [33 (link)].
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Publication 2016
Biofuels Biogas Cellulose Cereals Ethanol Fermentation Hypersensitivity Lignin Plants Steam Sugars Triticum aestivum
We selected a previously benchmarked dataset (Gerlach et al., 2009 ): the Biogas reactor dataset (Schlüter et al., 2008 (link)), composed of 353 213 reads of average 230 bp length. We selected a real dataset as opposed to a synthetic one because we did not want to tailor the dataset to any specific database, since the database will vary on each web site. This comparison fairly assesses each webserver's performance on a ‘real’ dataset containing known and novel organisms.
We conducted our tests against NBC and five other webservers in July and August of 2010. WebCARMA and MG-RAST require no parameters. Phylopythia requires the type of model to match against. MG-RAST requires an E-value cutoff under the SEED viewer (which we selected the highest). We selected default BLAST parameters for the NT database for Galaxy. For NBC, we used an Nmer size of 15 and the default 1032 organism genome-list. For CAMERA, we only retained the best top-hit organism for each read and used the ‘All Prokaryotes’ BLASTN database (and used the default parameters for the rest).
We implement the NBC approach in Rosen et al. (2008 ) that assigns each read a log-likelihood score. We introduce two functions of NBC: (i) the novice functionality and (ii) the expert functionality. We expect that most users will fit into the ‘novice’ category, which will enable them to upload their FASTA file of reads and obtain a file of summarized results matching each read to its most likely organism, given the training database. The parameters that (expert and novice) users can choose from are as follows:
Upload File: the FASTA formatted file of metagenomic reads. The webserver also accepts .zip, .gz and .tgz of several FASTA files.
Genome list: the algorithm speed depends linearly on the number of genomes that one scores against. So, if an expert user has prior knowledge about the expected microbes in the environment, he/she can select only those microbes that should be scored against. This will both speed up the computation time and reduce false positives of the algorithm.
Nmer length: the user can select different Nmer feature sizes, but it is recommended that the novice user use N = 15 since it works well for both long and short reads (Rosen et al., 2008 ).
Email: The user's email address is required so that they can be notified as to where to retrieve the results when the job is completed.
Output: For a beginner, we suggest to (i) upload a FASTA file with the metagenomic reads and (ii) enter an email address. The output is a link to a directory that contains your original upload file (renamed as userAnalysisFile.txt), the genomes that were scored against (masterGenomeList.txt) and a summary of the matches for each read (summarized_results.txt). The expert user may be particularly interested in the *.csv.gz files where he/she can analyze the ‘score distribution’ of each read more in depth.
Publication 2010
Biogas Genome Metagenome Prokaryotic Cells Radioallergosorbent Test
MetAMOS v1.5rc3 was executed using default settings. MG data were provided as input for single-omic assemblies (MetAMOS_MG) while MG and MT data were provided as input for multi-omic co-assemblies (MetAMOS_MGMT). All computations using MetAMOS were set to use eight computing cores (“-p 8”).
MOCAT v1.3 (MOCAT.pl) was executed using default settings. Paired-end MG data were provided as input for single-omic assemblies (MOCAT_MG) while paired-end MG and MT data were provided as input for multi-omic co-assemblies (MOCAT_MGMT). All computations using MOCAT were set to use eight computing cores (“-cpus 8”). Paired-end reads were first preprocessed using the read_trim_filter step of MOCAT (“-rtf”). For the human fecal microbiome datasets (HF1–5), the preprocessed paired- and single-end reads were additionally screened for human genome-derived sequences (“-s hg19”). The resulting reads were afterwards assembled with default parameters (“-gp assembly -r hg19”) using SOAPdenovo.
IMP v1.4 was executed for each dataset using different assemblers for the co-assembly step: i) default setting using IDBA-UD, and ii) MEGAHIT (“-a megahit”). Additionally, the analysis of human fecal microbiome datasets (HF1–5) included the preprocessing step of filtering human genome sequences, which was omitted for the wastewater sludge datasets (WW1–4) and the biogas (BG) reactor dataset. Illumina TruSeq2 adapter trimming was used for wastewater dataset preprocessing since the information was available. Computation was performed using eight computing cores (“- -threads 8”), 32 GB memory per core (“- -memcore 32”) and total memory of 256 GB (“- -memtotal 256 GB”). The customized parameters were specified in the IMP configuration file (exact configurations listed in the HTML reports [57 ]). The analysis of the CAMI datasets were carried using the MEGAHIT assembler option (“-a megahit”), while the other options remained as default settings.
In addition, IMP was also used on a small scale dataset to evaluate performance of increasing the number of threads from 1 to 32 and recording the runtime (“time” command). IMP was launched on the AWS cloud computing platform running the MEGAHIT as the assembler (“-a megahit”) with 16 threads (“- -threads 16”) and 122 GB of memory (“- -memtotal 122”).
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Publication 2016
Biogas Feces Genome, Human Human Microbiome Memory O(6)-Methylguanine-DNA Methyltransferase Sludge Strains
Strict anaerobic techniques were thoroughly applied in this study. Sterile anoxic bottles were prepared as described in Text S2 (Supplementary Materials) prior to medium dispensing and inoculation. The gas volume/liquid volume ratio was maintained at three for all experiments, regardless of the size of the bottle, unless stated otherwise. The experiments were conducted with four biological replicates in the first stage (gas feeding of the anaerobic sludge) and triplicates in the second stage (enrichment in the mineral medium). A detailed chronology of the culture transfers is provided in Table S4.
The setup in the first stage was assembled in an anaerobic chamber. Serum bottles of 219.5 mL volume were filled with 50 mL degassed inoculum, sealed with butyl rubber stoppers and crimped with aluminum caps. The gas phase of the serum bottles was replaced by H2 (80%) and CO2 (20%). All bottles receiving H2 and CO2 were operated in fed-batch mode and pressurized daily to ~2.2 bar for approximately five months. Bottles containing the inoculum and a nitrogen atmosphere (not pressurized) were used as controls to account for the residual biogas production. Detailed information about headspace flushing and pressurization is given in Text S2.
In the second stage, medium A was used to enrich a particle-free culture by six subsequent culture transfers in fresh medium bottles by inoculating the content of the preceding culture transfer (10%, v/v). One randomly selected replicate from the first stage served as the inoculum to start the bottles for the second stage. Anoxic medium A (45 mL) was dispensed to sterile, anoxic serum bottles and left overnight in an incubator at 37 °C to reduce any oxygen traces that entered the bottles during medium dispensing. Next, the bottles were inoculated with 5 mL culture from the first stage. Biological controls for determining residual biogas production (containing inoculum but with N2 gas phase), as well as sterile controls (not inoculated, but with either H2/CO2 or N2 gas phase), were also set up. The bottles were fed with a gaseous substrate, as described above, and incubated at 37.4 °C in an orbital shaking incubator (IKA KS 4000 ic control, IKA®-Werke GmbH & Co. KG, Biberach an der Riss, Germany) at 200 rpm.
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Publication 2020
Aluminum Anoxia Atmosphere Biogas Biopharmaceuticals butyl rubber DNA Replication Gases Minerals Nitrogen Oxygen Serum Sludge Sterility, Reproductive Vaccination
Data. We used the data from the WHO household energy database (WHO 2012b ), which is a systematic compilation of nationally representative surveys or censuses and builds on earlier versions developed by the University of California, Berkeley (Smith et al. 2004 ). The WHO database provides estimates of the percentage of households using as their primary cooking fuel solid fuels (coal, wood, charcoal, dung, and crop residues), liquid fuels (kerosene), gaseous fuels (liquid petroleum gas, natural gas, biogas), and electricity. About three-fourths of the data were disaggregated by individual fuel type and approximately two-thirds of the data by urban and rural residency. These estimates do not directly include fuels used for space heating.
These survey data were obtained from a variety of sources. International multicountry surveys, specifically Macro International’s Demographic and Health Surveys (U.S. Agency of International Development 2012 ), UNICEF’s Multiple Indicator Cluster Surveys (UNICEF 2012 ), the WHO’s World Health Surveys (WHO 2012c ), and the World Bank’s Living Standard Measurement Studies (World Bank 2012b ), which together account for 39% of data points in the database. National censuses constitute a further 18%, and other national surveys such as household, employment, living conditions, or expenditure surveys accounted for another 20% of the database. The remaining 23% of data points are from other sources, including environmental and poverty assessments, MDG reports, and statistical figures provided on the websites of national statistics bureaus.
A total of 586 national country-year data points were available for modeling. These data points covered 155 countries, including 97% of all low- and middle-income countries (LMIC; defined as having < US$12,276 per capita in 2011–2012) and territories between 1974 and 2010, with at least one survey per country. Further details are available in Supplemental Material, Table S1 (http://dx.doi.org/10.1289/ehp.1205987).
Methods for modeling household SFU at the national level. The aim of the modeling was to obtain a complete set of annual trends of primary SFU by country using a transparent, reproducible model. The model should be suitable for estimating SFU for years without survey information in a particular country, and for countries without any survey data. The model should also closely follow empirical data without being unduly influenced by large fluctuations in survey estimates of SFU over adjacent countries or years. This is important because large fluctuations are unlikely in practice and generally reflect (in addition to random error) differences in survey design and conduct. In the absence of data for certain periods, we borrowed information from regional trends, assuming that fuel use patterns are likely to be similar. Also, the model should not be unduly sensitive to parameters such as following the trends of covariates (e.g., gross national income per capita) without compelling evidence of similar trends in SFU.
As seen in other work estimating household SFU (Mehta et al. 2006 ), for countries with no solid-fuel data but that are classified as high-income countries according to the World Bank country classification (World Bank 2012a ), SFU was assumed to be < 5%.
We reviewed range of alternative modeling approaches, including a variety of linear regression models and Bayesian hierarchical/Gaussian process regression models [for details see Supplemental Material, pp. 2–3 (http://dx.doi.org/10.1289/ehp.1205987)]. Also, potential developmental and energy-related covariates thought to be related to household solid fuel use (e.g., gross national income per capita, the percentage of the total population living in rural areas, population density, the percentage of the total population with access to improved sanitation, and the percentage of total energy consumption from fossil fuels) were investigated.
Multilevel/mixed-effects model. A multilevel nonparametric model without covariates was selected because it best fulfilled the above criteria and provided the best fit to the data based on Akaike’s information criterion (AIC), the Bayesian information criterion (BIC), and visual inspection. Modeling assumptions—linearity, normality, and homoscedasticity—also were checked by visual inspection of the residuals and were reasonably met (Goldstein 2010 ; Hox 2010 ). All surveys were included in the model [see Supplemental Material, Table S1 (http://dx.doi.org/10.1289/ehp.1205987)]. Covariates (income, percentage of rural population, population density) were evaluated but not retained because trends in some countries were rather sensitive to the particular set of covariates used. Multilevel modeling takes into account the hierarchical structure of the data; for example, survey points are correlated within countries, which are then clustered within regions (Goldstein 2010 ). When information is scarce for a particular country, regional information is used to derive estimates for a country.
The 155 countries were grouped into the 21 GBD regions, which are based on geographical proximity and epidemiological similarity (IHME et al. 2009 ). The model included hierarchical random effects for regions and countries. Time was the only explanatory variable included in the model, both in terms of fixed and random effects (at country level). The time variable was centered at the year 2003 (the median date of the surveys) and transformed into a natural cubic spline to allow for nonlinearity while providing a desired degree of stability (Orsini and Greenland 2011 ; Peng et al. 2006 ). The number of knots for the spline was chosen to allow the model to adequately follow the survey point trend and avoid any unlikely fluctuation. The locations of the knots were determined by the percentiles of the independent variable (Harrell 2001 ). The covariance model was chosen to be unstructured.
Using a technique of statistical simulation described by King et al. (2000) , we computed the national SFU prevalence estimates and accounted for uncertainty. We drew 1,000 times from the model parameters for the fixed effects to generate the outcome variable in order to capture the estimation uncertainty. We used the method described by De Onis et al. (2004) (link) to derive regional and global prevalence confidence intervals (CIs).
We used the multilevel model for 150 countries with at least one survey data point. Regional estimates were used instead of model estimates for seven LMICs without survey data. We tested this assumption by performing out-of-sample evaluations on a truncated data set by removing countries from the data set (repeated 30 times). The mean median percentage point difference between the withheld data and the regional mean was 15.8%. We performed additional out-of-sample evaluations on three truncated data sets a) with 20% of the country-years withheld on countries with more than one survey (repeated 30 times), b) with the last survey withheld in countries with more than one survey and, c) with the last 3 years (2008–2010) withheld. The median percentage point differences between the withheld data and the model outputs were 3.7%, 3.6%, and 3.7%, respectively.
Calculation of the population exposed. The model derives estimates of the percentage of households using solid fuels for a particular country and year. The fraction of the population exposed was assumed to be the same as the fraction of households using solid fuels. Accordingly, the SFU fraction was multiplied by the national population (United Nations 2012b ) to obtain an estimate of the absolute population exposed per country. In other words, no attempt was made to adjust population estimates for variations in household size across various settings (e.g., urban vs. rural households) because such data were not consistently available.
All analyses were conducted using Stata software (version 12; StataCorp LP, College Station, TX, USA).
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Publication 2013
Biogas Charcoal Coal Crop, Avian Cuboid Bone Electricity Feces Head Households Kerosene Petroleum Rural Population

Most recents protocols related to «Biogas»

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Publication 2023
Biogas Flatulence Hybrids Marines Plasma Membrane Protons
A 7 L lab-scale
bioreactor with a working volume of 5 L was operated semi-continuously
as an anaerobic sequencing batch reactor (ASBR) for 339 days. The
ASBR was run on a 24 h cycle through four cycles: (1) feeding (8–10
min), (2) react phase with continuous mixing and pH adjustment (22
h 40 min), (3) settling (1 h), and (4) decanting for withdrawal of
effluent equal to the volume of the influent fed (8–10 min).
The bioreactor was temperature controlled at 40 ± 0.5 °C
until Day 73 and at 37 ± 0.5 °C from Days 74 to 339. The
bioreactor pH was maintained at 5.5 ± 0.1 by the automatic addition
of 3 M NaOH with the help of LabVIEW (National Instruments, Austin,
TX). The biogas was collected in a 5 L Tedlar gas bag. Rumen content
(17.1 ± 1.0 g volatile solids (VS) L–1), obtained
from a fistulated cow from a dairy farm at Michigan State University
(East Lansing, MI), was used as an inoculum. The bioreactor was operated
at a hydraulic retention time (HRT) of 2–4 days and an organic
loading rate (OLR) of (10.5 ± 7.0 g soluble chemical oxygen demand
(sCOD) L–1 d–1). The solids retention
time (SRT) was controlled around 9.7 ± 5.8 days from Days 20
to 81 by wasting suspended biomass from the bioreactor (during the
react phase) and effluent (after the decant phase). The volatile suspended
solids concentrations in both suspended biomass and effluent were
considered for SRT calculation. Additional operational details are
described by Shrestha et al.3 (link)A mixture
of waste beer containing ethanol and permeate extracted from an acidogenic
bioreactor20 treating food waste was fed
to the ASBR once a day. The influent was prepared once a week. Waste
beer was obtained from Jolly Pumpkin Brewery (Dexter, MI), where it
represents 2–19% of the total volumetric beer production (Doug
Knox, Sustainability Manager, personal communication). The sodium
salt of 2-BES (Sigma-Aldrich, St. Louis, MO) was added to the ASBR
at the beginning of the react phase roughly every 2 weeks, the first
two times on Days 230 and 246, and every 10 days (equivalent to approximately
three HRTs) after that on Days 259, 269, 278, 287, 296, 305, and 314
to reach a bioreactor concentration of 10 mM (∼10.8 g in 5
L working volume of the bioreactor) immediately after each addition.
The 2-BES dose was selected based on literature values obtained from
anaerobic mixed-culture studies.21 (link),22 (link) The change
in 2-BES concentration over time was estimated using the initial concentration
added, the volume of effluent wasted per day, and the bioreactor working
volume. Thermodynamic calculations were performed to evaluate the
feasibility of different reactions during the period 2-BES was added
(details are given in the Supporting Information [SI]).
Publication 2023
austin BAG5 protein, human Beer Biogas Bioreactors Bos taurus Chemical Oxygen Demand Ethanol Food Pumpkins Retention (Psychology) Rumen Tedlar Therapy, Hormone Replacement
The pH and temperature were monitored monthly using a pH meter (Sartorius PB-10) and a thermometer separately. The different organic loading rates (OLRs) were achieved by various chemical oxygen demand (COD) concentrations at a fixed hydraulic retention time (HRT). The COD, total suspended solids (TSS), and volatile suspended solids (VSS) were measured according to standard methods (Rice et al., 2012 ). Biogas production was monthly monitored and the CH4 percentage was determined by Gas Chromatography (SRI 8610 C). The ammonium nitrogen and total nitrogen concentration were determined by the SmartChem Discrete Auto Analyzer (Smartchem200, AMS-Westco, Italy) and Shimadzu TOC Analyzer (TOC-Vcsh; Shimadzu), respectively.
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Publication 2023
Ammonium Biogas Chemical Oxygen Demand Gas Chromatography Nitrogen Oryza sativa Retention (Psychology) Thermometers
The biocontrol strains, isolated from pig biogas slurry, were obtained from the Institute of Plant Protection, Liaoning Academy of Agricultural Sciences. S. rolfsii was provided by the College of Plant Protection, Shenyang Agricultural University. PHT0-P43GFPmut3a, a plasmid carrying chloramphenicol-and green fluorescent protein-encoding genes, was provided by the Rice Disease Research Laboratory, Institute of Plant Protection, Liaoning Academy of Agricultural Sciences. A peanut rot susceptible variety of the Fuyu four red peanut (Fan, 2021 ) was used for the analysis (Registration Number: GPD [2018]220156).
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Publication 2023
Arachis hypogaea Beriberi Biogas Chloramphenicol Genes Green Fluorescent Proteins Plants Plasmids Strains
BSF larvae were originally obtained from Bio.S Biogas (Grimma, Germany) in July 2018. Since then, the population has been genetically isolated (~30 generations) from others and reared continuously on chicken feed (GoldDott Eierglück, DERBY Spezialfutter, Muenster, Germany), which is frequently used as a high-quality diet [26 (link)]. The larvae were maintained in 19.5 × 16.5 × 9.5 cm (l × w × h) polypropylene boxes with 150 mg eggs (~6000 eggs) per box at 27 ± 1 °C and 65 ± 5% relative humidity in constant darkness [27 (link),28 (link),29 ]. Once ≥50% of the colony had reached the sixth instar, dark-colored prepupae were separated from the substrate using a vibratory sieve shaker (AS 200, Retsch, Haan, Germany). For pupation and subsequent metamorphosis, prepupae were transferred to mesh cages (Bioform, Nuremberg, Germany), each with a size of 60 × 60 × 90 cm (l × w × h), located in the greenhouse.
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Publication 2023
Biogas Biological Metamorphosis Chickens Darkness Diet Eggs Humidity Larva Polypropylenes Vibration

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More about "Biogas"

Biogas is a versatile renewable energy source that is gaining increasing attention as a sustainable alternative to traditional fossil fuels.
Produced through the anaerobic digestion of organic matter, such as agricultural waste, animal manure, and municipal solid waste, biogas is primarily composed of methane (CH4) and carbon dioxide (CO2).
This clean energy solution offers numerous benefits, including waste management and reduced reliance on non-renewable resources.
Biogas can be utilized in a variety of applications, including heating, electricity generation, and transportation.
The composition and quality of biogas can be analyzed and optimized using advanced analytical instruments like the GC-2014, Clarus 580, GC-2010, 490 Micro GC, GC-8A, GC-2014C, and Agilent 6890N gas chromatographs, as well as the TOC-VCPH total organic carbon analyzer.
These tools can help researchers and developers identify the most reliable protocols and enhance the reproducibility and accuracy of biogas projects.
Advancements in sequencing technologies, such as the HiSeq 2000, have also enabled researchers to better understand the microbial communities involved in the anaerobic digestion process, which is crucial for optimizing biogas production.
By leveraging the power of AI-driven platforms like PubCompare.ai, researchers can efficiently navigate the scientific literature, preprints, and patents to identify the most reliable protocols and methodologies, ultimately improving the efficiency and sustainability of biogas production.
Whether you're a researcher, engineer, or industry professional, exploring the potential of biogas as a renewable energy source can lead to exciting opportunities for innovation and environmental stewardship.
With the right tools and resources, you can unlock the full potential of this versatile and sustainable energy solution.