نتایج جستجو برای: moving bed bio reactor

تعداد نتایج: 237366  

Journal: :Bioresource technology 2013
Anqing Zheng Zengli Zhao Sheng Chang Zhen Huang Xiaobo Wang Fang He Haibin Li

Pretreatment of corncobs using torrefaction was conducted in an auger reactor at 250-300 °C and residence times of 10-60 min. The torrefied corncobs were fast pyrolyzed in a bubbling fluidized bed reactor at 470 °C to obtain high-quality bio-oil. The heating value and pH of the bio-oil improved when the torrefaction as pretreatment was applied; however, increasing bio-oil yield penalties were o...

Journal: :iranian journal of health sciences 0
mehdi ahmadi environmental technology research center and department of environmental health engineering, ahvaz jundishapur university of medical sciences, ahvaz, iran aliakbar mehr alian department of environmental engineering, bandar abbas science and research branch, islamic azad university, bandar abbas. iran hoda amiri department of environmental health engineering, tehran university of medical sciences, tehran, iran bahman ramavandi department of environmental health engineering, faculty of health, bushehr university of medical sciences, bushehr, iran hassan izanloo department of environmental health engineering, research center for environment pollutants, qom university of medical sciences, qom, iran

background and purpose: the performance of full-scale moving bed biofilm reactor (mbbr) was evaluated as an alternative for upgrading of kish island mirmohana wastewater treatment plant. in this study activated sludge process upgrade to mbbr process and different operating parameters were compared. materials and methods: effect of upgrading on different parameters such as organic loading rate (...

2008
Fei Wang Fanxing Li Andrew Tong Deepak Sridhar Liang-Shih Fan

The syngas chemical looping (SCL) process developed at the Ohio State University can efficiently convert coal derived syngas into hydrogen with in-situ CO2 capture. In this novel process, two moving bed units are used to convert syngas into hydrogen through the assistance of an oxygen carrier particle. A third unit, an entrained bed combustor, is used to convey the oxygen carrier particles to c...

2012
G. AROCA M. CÁCERES S. PRADO C. SÁNCHEZ

The odour generated by industrial gaseous emissions causing nuisances generally is due to the presence of volatile reduced sulfur compounds (VRSC) Although a number of microorganisms are known for degrading VRSC, the treatment of a mixture of reduced sulfur compounds remains challenging for several reasons. To resolve these problems two-stage systems have been proposed, in the first reactor H 2...

Ali Babaei Mehdi Ahmadi Mehdi Vosoughi Niri Nadali Alavi Nemat Jafarzadeh Zeinab Baboli zeinab ghaedrahmat,

Background: Phenolic compounds are found in wastewater of many industries such as pulp and paper, textile, petrochemical, oil refineries, production of phenolic resins, plastics, coal furnace, tannery, rubber reclamation plant, fertilizers, coke, paints, rubber, decolorizer, resins, rubber and phenol- formaldehyde resin industries. This study aimed to evaluate Moving Bed Biofil...

2007
P. N. Kechagiopoulos S. S. Voutetakis A. A. Lemonidou I. A. Vasalos

Hydrogen produced from renewable energy sources can present significant environmental benefits as an alternative to fossil fuels or as a means for clean power generation via fuel cells. The aqueous fraction of bio oil can be used as a source for hydrogen production, if reformed in the presence of active catalytic materials. Recently, we introduced the concept of the spouted bed reactor for the ...

2011
Jean-Luc Vasel

Problem statement: Nitrification by Moving Bed Biofilm Reactor (MBBR) involves physical, chemical and biological processes to remove toxic ammonia for aquaculture that are governed by a variety of parameters, like substrate and dissolved oxygen concentrations, organic matters, temperature, pH, alkalinity and turbulence level, which impact negatively or positively on nitrification kinetics. App...

Journal: :Korean Chemical Engineering Research 2011

2010
Mohammad Rofiqul ISLAM Hiroyuki HANIU Mohammad Nurul ISLAM Md. Shazib UDDIN

Thermochemical conversion of sugarcane bagasse into bio-crude oils by fluidized-bed reactor has been taken into consideration in this study. The bagasse in particle form was pyrolyzed in an externally heated 7cm diameter and 37.5cm high fluidized-bed reactor with nitrogen as a carrier gas. The reactor chamber and gas-preheater were heated by means of a renewable energy biomass source cylindrica...

2014
Jae Hyung Choi Hee Chul Woo Dong Jin Suh

A pyrolysis study on a species of brown algae Saccharina japonica was carried out in a fixed-bed reactor. The yields of bio-oil and bio-char obtained at 450 C were 47 % and 33 %, respectively. The raw S, japonica, ethanol and acid pretreated samples and the resulting pyrolysis products were also characterized with respect to proximate and ultimate analysis, and higher heating value. The crude b...

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