دانلود مقاله ISI انگلیسی شماره 28218
عنوان فارسی مقاله

تجزیه و تحلیل سیستم تبدیل به گاز نوشابه سیاه خشک مبتنی بر تولید گاز مصنوعی در مقایسه با اکسیژن و هوا دمیده سیستم های تبدیل به گاز

کد مقاله سال انتشار مقاله انگلیسی ترجمه فارسی تعداد کلمات
28218 2013 8 صفحه PDF سفارش دهید محاسبه نشده
خرید مقاله
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عنوان انگلیسی
System analysis of dry black liquor gasification based synthetic gas production comparing oxygen and air blown gasification systems
منبع

Publisher : Elsevier - Science Direct (الزویر - ساینس دایرکت)

Journal : Applied Energy, Volume 112, December 2013, Pages 1275–1282

کلمات کلیدی
تبدیل به گاز نوشابه سیاه - گردشی بستر سیال - گاز طبیعی مصنوعی
پیش نمایش مقاله
پیش نمایش مقاله تجزیه و تحلیل سیستم تبدیل به گاز نوشابه سیاه خشک مبتنی بر تولید گاز مصنوعی در مقایسه با اکسیژن و هوا دمیده سیستم های تبدیل به گاز

چکیده انگلیسی

The black liquor gasification based bio-fuel production at chemical pulp mill is an attractive option to replace conventional recovery boilers increasing system energy efficiency. The present paper studies circulating fluidized bed system with direct causticization using TiO2 for the gasification of the black liquor to the synthesis gas. The advantage of using direct causticization is the elimination of energy-intensive lime kiln which is an integral part of the conventional black liquor recovery system. The study evaluates the effects of gasifying medium i.e. oxygen or air, on the fluidized bed gasification system, the synthesis gas composition, and the downstream processes for the synthesis gas conversion to the synthetic natural gas (SNG). The results showed higher synthetic natural gas production potential with about 10% higher energy efficiency using oxygen blown gasification system than the air blown system. From the pulp mill integration perspective, the material and energy balance results in better integration of air blown system than the oxygen blown system, e.g. less steam required to be generated in the power boiler, less electricity import, and less additional biomass requirement. However, the air blown system still requires a significant amount of energy in terms of the synthesis gas handling and gas upgrading using the nitrogen rejection system.

مقدمه انگلیسی

1.1. Background According to Energy Information Administration, the fossil fuel consumption is expected to expand by 50% from 2005 to 2030 that would raise issues like greenhouse gas (GHG) emissions and future fuel security [1]. In future energy systems, bio-fuels replacing fossil fuels are considered to play a vital role due to GHG reduction policies. The European Union (EU) in renewable directive 2009 has set a target of 20% of energy supplied in EU shall come from renewable energy resources by 2020 [2]. As per the directive, the share of bio-fuels in the transport sector shall be 10% [2]. Sweden has set a goal of introducing 50% of the energy supplied shall come from the renewable energy resources by 2020 [2]. To meet such challenging targets, a large scale bio-fuel production would consume a substantial amount of bio-resources especially forest-based biomass. This leads to a very efficient use of biomass. The pulp and paper industry has a potential to become a bio-refinery, as a key producer of bio-fuels in future energy systems due to an established infrastructure. The pulp and paper industry can co-produce pulp and paper products together with different types of bio-fuels, e.g. synthetic natural gas (SNG), dimethyl ether (DME), or methanol, etc., using black liquor gasification technology. Black liquor (BL) is a major energy resource in countries with large pulp and paper industry, e.g. about 40 TW h of energy is available in the form of black liquor in Sweden [2]. Black liquor, spent cooking liquor, contains lignin obtained after the delignification process from the wood and in-organic cooking chemicals used for the delignification process. In conventional pulp mills, black liquor is fired in the recovery boilers to generate steam and electricity for pulp mill operations. The in-organic chemicals are recovered to re-use in the delignification process. However, black liquor can be gasified to the synthesis gas containing CO, H2, and CH4 as raw constituents for various bio-fuel production alternatives increasing overall energy efficiency of the mill. Among various alternatives, the synthetic natural gas (SNG) production is an interesting option to reduce natural gas dependency and associated GHG emissions. The black liquor gasification (BLG) route to SNG could be advantageous in terms of fuel security, current fuel supply infrastructure, and in a wide range of industrial applications. A basic concept of bio-fuel production at the pulp mill as a bio-refinery is shown in Fig. 1. Figure options 1.2. Previous studies A number of studies have been made previously to investigate the most efficient route for the production of bio-fuel using different black liquor gasification technologies as a replacement of the conventional black liquor recovery cycle, e.g. DARS process, SCA-Billerud process, dry BLG with direct causticization, Manufacturing and Technology Conversion International process, and Chemrec gasification process [3], [4], [5], [6], [7] and [8]. The combined heat and power concept and various power cycles with black liquor gasification integrated with the pulp and paper mill haven been analyzed [9] and [10]. The studies on the consequences of various bio-fuel alternatives as transport fuels replacing petroleum fuels using Chemrec black liquor gasification process resulted in substantial improvement in the pulp and paper mill energy system [11], [12], [13], [14] and [15]. The hydrothermal gasification system using supercritical oxidation process for direct methane production was proposed and showed a large potential of SNG production from wet biomass [16], [17] and [18]. The dry black liquor gasification system with direct causticization using titanium dioxide (TiO2) is experimentally analyzed using air as gasifying medium [19], [20] and [21]. 1.3. Objective and motivation In a conventional circulating fluidized bed (CFB), air is generally used as a gasifying medium diluting the produced synthesis gas with a high concentration of nitrogen. This lowers the heating value of the synthesis gas due to dilution with nitrogen which cannot be easily separated from the synthetic natural gas. However if oxygen is used for the gasification process, there is an increased possibility of bed material agglomeration due to the formation of local hot spots in the gasification zone. The present paper addresses reduced risk of agglomeration formation in the case of black liquor as raw material for the synthesis gas production in oxygen blown circulating fluidized bed (CFB) gasifier as compared to other conventional biomass resources. This paper is continuation of our previous published research work on black liquor gasification based bio-refinery systems [15], [17], [32], [33] and [34]. The study compares energy conversion performance of black liquor to the synthetic natural gas (SNG) from air blown dry black liquor gasification system i.e. termed as DBLG (air), with oxygen blown dry black liquor gasification system i.e. termed as DBLG (O2). The dry black liquor gasification system with direct causticization is used integrated with a reference pulp mill producing 1000 air-dried tonnes (ADts) of pulp per day. The comparative results are presented as differences in the overall material and energy balances, the synthetic natural gas (SNG) production potential, energy ratios, and potential CO2 reductions combining on-site CO2 reduction together with CO2 offsets from the SNG replacing gasoline in the transport sector. The study emphasizes to keep pulping process identical to conventional pulping process and to recover in-organic chemicals for re-use in the delignification process.

نتیجه گیری انگلیسی

This paper compared two dry black liquor gasification systems with direct causticization for the synthetic natural gas production based on different gasifying agents i.e. air or oxygen. The study showed better system integration of gasification with oxygen based on results from energy performance indicators. The risk of agglomeration formation in the bed material of the oxygen blown circulating fluidized bed gasifier could be significantly reduced due to the water content of the black liquor. Based on the reference mill capacity, the SNG production potential is considerably higher in the oxygen blown DBLG system (about 162 MW) than the air blown DBLG system (about with 64 MW). In addition, about 700 and 300 kilo tonnes per year of CO2 reductions could be achieved in the DBLG (O2) system and the DBLG (air) system respectively, i.e. both possible CO2 capture and CO2 offset from the SNG replacing the natural gas.

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