Upper Austria Green Biorefinery - Revision history

Poli: merged as example with http://opensourceecology.org/wiki/Biorefinery

2012-06-07T11:23:36Z

merged as example with http://opensourceecology.org/wiki/Biorefinery

← Older revision		Revision as of 11:23, 7 June 2012
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	~~{{Category=Materials}}~~		''Merged as example with http://opensourceecology.org/wiki/Biorefinery.''

	~~{{Category=Biofuel}}~~

	~~{{Category=Bioplastics}}~~

	''~~'Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria~~
	~~'''<br>~~
	~~J. Ecker, 1M. Harasek<br>~~
	~~Vienna University of Technology, Institute of Chemical Engineering, Getreidemarkt 9/166-2, 1060 Wien, Tel.: +43-1-58801-15978, <br>~~
	~~e-mail: jecker@mail.zserv.tuwien.ac.at; <br>~~
	~~Vienna University of Technology, Institute of Chemical Engineering, Getreidemarkt 9/166-2, <br>~~
	~~e-mail: michael.harasek@tuwien.ac.at<br>~~

	~~source:~~
	~~[http://www.chisa.cz/2010/admin/contrib_get_abstract_edited.asp?id_02=1121 here]~~

	~~Within the project [~~http://~~www~~.~~energytech.at~~/~~pdf~~/~~biorefinery_steinmueller.pdf "Green~~ Biorefinery ~~Upper Austria"] a demonstration plant for the separation of resources from grass [[silage]] was built up and operated near the [[biogas]] plant in Utzenaich (Upper Austria)~~. The aim of the project, which includes the OÖ Bioraffinerie GesmbH, Joanneum Research Forschungsgesellschaft mbH and BiorefSys as partners, is to produce lactic acid and various amino acids from pressed silage juice.

	The juice is pressed from silage bales of farmers in the vicinity of the bio-refinery. The material varies from normal grass to special grass clovers, which contain higher amounts of potential resources. After sedimentation, the process (Figure 1) is started with the production of the acid containing streams. The first step is an ultrafiltration unit in which disturbing macromolecules and proteins can be separated from the product stream. After this first clarification step the stream is fed into a nanofiltration unit. This standard unit operation allows the separation of phases enriched in amino acids and phases enriched in lactic acid. The divided streams are processed in two separated ways. The phase loaded with amino acids is cleared in an ion exchange street. Streams having concentrated amounts of specific amino acids fractions are produced in this step. The lactic acid stream is fed into two serial electrodialysis units. In the first unit the stream is desalinated. The varying amount of salts in the feed can be compensated with different dwell times. The salts are migrating into the concentrate cycle, which is the waste stream of this step. The desalinated stream is fed into a reverse osmosis plant to increase the amount of lactic acid and to reduce the volume to be pumped. The concentrated stream is the feed for the second electrodialysis unit, which separates the lactic acid from the diluate. Due to its structure, the acid is migrating slowly. The transport can be enhanced by increasing the current density and the dwelling time in the tanks. One of the most important advantages of the “Green Biorefinery” is that no waste is produced. All of the accumulated by-products, i.e. press-cake, ultrafiltration-retentate and electrodialysis concentrate, can be used as substrates in the adjacent biogas plant Utzenaich. The other product free streams are recycled in the “Green Biorefinery” itself.

	The product streams will be used for different applications. For example, there are uses of lactic acid in the animal food industry or in the chemical industry as a precursor of ethyl lactate. The amino acids are used in the food industry or in cosmetics and pharma industry. This process still needs improvements to achieve high product quality to be less dependent on the raw materials. In the 30 month duration of the project the procedure will be optimized and, if necessary, changes are made in the build up to produce economic products.

	Within this work, first process results of the electrodialysis systems for the lactic acid production will be presented. Additionally, initial system performance and first operating experiences during continuous campaigns will be reported.

	[[File:Upper Austria Green Biorefinery - Figure 1.JPG\|500px\|thumb\|left\|Figure 1: Process flow diagram (Source: Fabrik der Zukunft GmbH, Federal Ministry of Transport, Innovation and Technology, translated by the author)
	]]

Rasmus: inserted links

2011-02-28T15:57:59Z

inserted links

← Older revision		Revision as of 15:57, 28 February 2011
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	[http://www.chisa.cz/2010/admin/contrib_get_abstract_edited.asp?id_02=1121 here]		[http://www.chisa.cz/2010/admin/contrib_get_abstract_edited.asp?id_02=1121 here]

	Within the project "Green Biorefinery Upper Austria" a demonstration plant for the separation of resources from grass silage was built up and operated near the biogas plant in Utzenaich (Upper Austria). The aim of the project, which includes the OÖ Bioraffinerie GesmbH, Joanneum Research Forschungsgesellschaft mbH and BiorefSys as partners, is to produce lactic acid and various amino acids from pressed silage juice.		Within the project [http://www.energytech.at/pdf/biorefinery_steinmueller.pdf "Green Biorefinery Upper Austria"] a demonstration plant for the separation of resources from grass [[silage]] was built up and operated near the [[biogas]] plant in Utzenaich (Upper Austria). The aim of the project, which includes the OÖ Bioraffinerie GesmbH, Joanneum Research Forschungsgesellschaft mbH and BiorefSys as partners, is to produce lactic acid and various amino acids from pressed silage juice.

	The juice is pressed from silage bales of farmers in the vicinity of the bio-refinery. The material varies from normal grass to special grass clovers, which contain higher amounts of potential resources. After sedimentation, the process (Figure 1) is started with the production of the acid containing streams. The first step is an ultrafiltration unit in which disturbing macromolecules and proteins can be separated from the product stream. After this first clarification step the stream is fed into a nanofiltration unit. This standard unit operation allows the separation of phases enriched in amino acids and phases enriched in lactic acid. The divided streams are processed in two separated ways. The phase loaded with amino acids is cleared in an ion exchange street. Streams having concentrated amounts of specific amino acids fractions are produced in this step. The lactic acid stream is fed into two serial electrodialysis units. In the first unit the stream is desalinated. The varying amount of salts in the feed can be compensated with different dwell times. The salts are migrating into the concentrate cycle, which is the waste stream of this step. The desalinated stream is fed into a reverse osmosis plant to increase the amount of lactic acid and to reduce the volume to be pumped. The concentrated stream is the feed for the second electrodialysis unit, which separates the lactic acid from the diluate. Due to its structure, the acid is migrating slowly. The transport can be enhanced by increasing the current density and the dwelling time in the tanks. One of the most important advantages of the “Green Biorefinery” is that no waste is produced. All of the accumulated by-products, i.e. press-cake, ultrafiltration-retentate and electrodialysis concentrate, can be used as substrates in the adjacent biogas plant Utzenaich. The other product free streams are recycled in the “Green Biorefinery” itself.		The juice is pressed from silage bales of farmers in the vicinity of the bio-refinery. The material varies from normal grass to special grass clovers, which contain higher amounts of potential resources. After sedimentation, the process (Figure 1) is started with the production of the acid containing streams. The first step is an ultrafiltration unit in which disturbing macromolecules and proteins can be separated from the product stream. After this first clarification step the stream is fed into a nanofiltration unit. This standard unit operation allows the separation of phases enriched in amino acids and phases enriched in lactic acid. The divided streams are processed in two separated ways. The phase loaded with amino acids is cleared in an ion exchange street. Streams having concentrated amounts of specific amino acids fractions are produced in this step. The lactic acid stream is fed into two serial electrodialysis units. In the first unit the stream is desalinated. The varying amount of salts in the feed can be compensated with different dwell times. The salts are migrating into the concentrate cycle, which is the waste stream of this step. The desalinated stream is fed into a reverse osmosis plant to increase the amount of lactic acid and to reduce the volume to be pumped. The concentrated stream is the feed for the second electrodialysis unit, which separates the lactic acid from the diluate. Due to its structure, the acid is migrating slowly. The transport can be enhanced by increasing the current density and the dwelling time in the tanks. One of the most important advantages of the “Green Biorefinery” is that no waste is produced. All of the accumulated by-products, i.e. press-cake, ultrafiltration-retentate and electrodialysis concentrate, can be used as substrates in the adjacent biogas plant Utzenaich. The other product free streams are recycled in the “Green Biorefinery” itself.

Conor at 15:57, 28 February 2011

2011-02-28T15:57:16Z

← Older revision		Revision as of 15:57, 28 February 2011
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	{{Category=Materials}}		{{Category=Materials}}

	{{Category=Biofuel}}		{{Category=Biofuel}}

	{{Category=Bioplastics}}		{{Category=Bioplastics}}

Rasmus: more categorization

2011-02-28T15:51:18Z

more categorization

← Older revision		Revision as of 15:51, 28 February 2011
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	{{Category:Materials}}		{{Category=Materials}}
			{{Category=Biofuel}}
			{{Category=Bioplastics}}

	'''Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria		'''Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria

Rasmus at 15:48, 28 February 2011

2011-02-28T15:48:23Z

← Older revision		Revision as of 15:48, 28 February 2011
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	{{Category:Materials}}		{{Category:Materials}}


	'''Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria		'''Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria
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	e-mail: michael.harasek@tuwien.ac.at<br>		e-mail: michael.harasek@tuwien.ac.at<br>

			source:
			[http://www.chisa.cz/2010/admin/contrib_get_abstract_edited.asp?id_02=1121 here]

	Within the project "Green Biorefinery Upper Austria" a demonstration plant for the separation of resources from grass silage was built up and operated near the biogas plant in Utzenaich (Upper Austria). The aim of the project, which includes the OÖ Bioraffinerie GesmbH, Joanneum Research Forschungsgesellschaft mbH and BiorefSys as partners, is to produce lactic acid and various amino acids from pressed silage juice.		Within the project "Green Biorefinery Upper Austria" a demonstration plant for the separation of resources from grass silage was built up and operated near the biogas plant in Utzenaich (Upper Austria). The aim of the project, which includes the OÖ Bioraffinerie GesmbH, Joanneum Research Forschungsgesellschaft mbH and BiorefSys as partners, is to produce lactic acid and various amino acids from pressed silage juice.

Rasmus: Created page with "{{Category:Materials}} '''Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria '''
J. Ecker, 1M. Harasek
Vienna University of T..."

2011-02-28T15:44:09Z

Created page with "{{Category:Materials}} '''Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria ''' J. Ecker, 1M. Harasek Vienna University of T..."

New page

{{Category:Materials}}

'''Membrane based production of lactic acid and amino acids – green biorefinery Upper Austria
''' 
J. Ecker, 1M. Harasek 
Vienna University of Technology, Institute of Chemical Engineering, Getreidemarkt 9/166-2, 1060 Wien, Tel.: +43-1-58801-15978, 
e-mail: jecker@mail.zserv.tuwien.ac.at; 
Vienna University of Technology, Institute of Chemical Engineering, Getreidemarkt 9/166-2, 
e-mail: michael.harasek@tuwien.ac.at 

Within the project "Green Biorefinery Upper Austria" a demonstration plant for the separation of resources from grass silage was built up and operated near the biogas plant in Utzenaich (Upper Austria). The aim of the project, which includes the OÖ Bioraffinerie GesmbH, Joanneum Research Forschungsgesellschaft mbH and BiorefSys as partners, is to produce lactic acid and various amino acids from pressed silage juice.

The juice is pressed from silage bales of farmers in the vicinity of the bio-refinery. The material varies from normal grass to special grass clovers, which contain higher amounts of potential resources. After sedimentation, the process (Figure 1) is started with the production of the acid containing streams. The first step is an ultrafiltration unit in which disturbing macromolecules and proteins can be separated from the product stream. After this first clarification step the stream is fed into a nanofiltration unit. This standard unit operation allows the separation of phases enriched in amino acids and phases enriched in lactic acid. The divided streams are processed in two separated ways. The phase loaded with amino acids is cleared in an ion exchange street. Streams having concentrated amounts of specific amino acids fractions are produced in this step. The lactic acid stream is fed into two serial electrodialysis units. In the first unit the stream is desalinated. The varying amount of salts in the feed can be compensated with different dwell times. The salts are migrating into the concentrate cycle, which is the waste stream of this step. The desalinated stream is fed into a reverse osmosis plant to increase the amount of lactic acid and to reduce the volume to be pumped. The concentrated stream is the feed for the second electrodialysis unit, which separates the lactic acid from the diluate. Due to its structure, the acid is migrating slowly. The transport can be enhanced by increasing the current density and the dwelling time in the tanks. One of the most important advantages of the “Green Biorefinery” is that no waste is produced. All of the accumulated by-products, i.e. press-cake, ultrafiltration-retentate and electrodialysis concentrate, can be used as substrates in the adjacent biogas plant Utzenaich. The other product free streams are recycled in the “Green Biorefinery” itself.

The product streams will be used for different applications. For example, there are uses of lactic acid in the animal food industry or in the chemical industry as a precursor of ethyl lactate. The amino acids are used in the food industry or in cosmetics and pharma industry. This process still needs improvements to achieve high product quality to be less dependent on the raw materials. In the 30 month duration of the project the procedure will be optimized and, if necessary, changes are made in the build up to produce economic products.

Within this work, first process results of the electrodialysis systems for the lactic acid production will be presented. Additionally, initial system performance and first operating experiences during continuous campaigns will be reported.

[[File:Upper Austria Green Biorefinery - Figure 1.JPG|500px|thumb|left|Figure 1: Process flow diagram (Source: Fabrik der Zukunft GmbH, Federal Ministry of Transport, Innovation and Technology, translated by the author)
]]