Desalination - Team E - Revision history

Jstolley: /* Appendix 6: Economic Anlaysis */

2016-03-12T05:59:51Z

Appendix 6: Economic Anlaysis

← Older revision		Revision as of 05:59, 12 March 2016
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	===Case I ===		===Case I ===
	Water is $700; RO with 1 stage and 5 elements		Water is $700; RO with 1 stage and 5 elements
	[[File:~~Appendix_6_C1~~.png\|center]]		[[File:C1.png\|center\|frame]]
	<br />		<br />

	===Case II===		===Case II===
	Water is $1400; RO with 1 stage and 5 elements		Water is $1400; RO with 1 stage and 5 elements
	[[File:~~Appendix_6_C2~~.png\|center]]		[[File:C2.png\|center\|frame]]
	<br />		<br />

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	===Case IV: Breakeven (NPV = 0 at 10 years)===		===Case IV: Breakeven (NPV = 0 at 10 years)===
	Water is $2104; RO with 1 stage and 5 elements		Water is $2104; RO with 1 stage and 5 elements
	[[File:~~Appendix_6_C4~~.png\|center]]		[[File:C4.png\|center\|frame]]
	<br />		<br />

	===Case V: Breakeven (NPV = 0 at 10 years)===		===Case V: Breakeven (NPV = 0 at 10 years)===
	Water is $2112; RO with 2 stages and 5,5 elements		Water is $2112; RO with 2 stages and 5,5 elements
	[[File:~~Appendix_6_C5~~.png\|center]]		[[File:C5.png\|center\|frame]]
	<br />		<br />

	===Case VI: Breakeven (NPV = 0 at 10 years)===		===Case VI: Breakeven (NPV = 0 at 10 years)===
	Water is $2138 with 1 stage and 1 element		Water is $2138 with 1 stage and 1 element
	[[File:~~Appendix_6_C6~~.png\|center]]		[[File:C6.png\|center\|frame]]
	<br />		<br />


	==Appendix 7: ROSA Simulation Outputs==		==Appendix 7: ROSA Simulation Outputs==

Jstolley: /* Appendices */

2016-03-12T05:51:03Z

Appendices

← Older revision		Revision as of 05:51, 12 March 2016
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	==Appendix 1: Design Basis==		==Appendix 1: Design Basis==
	[[File:Appendix_1.png\|center\|Appendix_1.png]]		[[File:Appendix_1.png\|center\|Appendix_1.png]]
			<br />

	==Appendix 2: Process Flow Diagram==		==Appendix 2: Process Flow Diagram==
	[[File:Appendix_2.png\|center\|frame]]		[[File:Appendix_2.png\|center\|frame]]
			<br />

	==Appendix 3: Mass and Energy Balance Tables==		==Appendix 3: Mass and Energy Balance Tables==
	'''Table 1'''. Mass balance on 1 stage 5 element RO system, where "out" is the sum of all the concentrate and permeate.		'''Table 1'''. Mass balance on 1 stage 5 element RO system, where "out" is the sum of all the concentrate and permeate.
	[[File:Appendix_3_T1.png\|center\|500px\|]]		[[File:Appendix_3_T1.png\|center\|500px\|]]
			<br />

	'''Table 2'''. Mass balance on 1 stage 1 element RO system, where "out" is the sum of all the concentrate and permeate.		'''Table 2'''. Mass balance on 1 stage 1 element RO system, where "out" is the sum of all the concentrate and permeate.
	[[File:Appendix_3_T2.png\|center\|500px\|]]		[[File:Appendix_3_T2.png\|center\|500px\|]]
			<br />

	'''Table 3'''. Mass balance on 2 stage 5,5 element RO system, where "out" is the sum of all the concentrate and permeate.		'''Table 3'''. Mass balance on 2 stage 5,5 element RO system, where "out" is the sum of all the concentrate and permeate.
	[[File:Appendix_3_T3.png\|center\|600px\|]]		[[File:Appendix_3_T3.png\|center\|600px\|]]
			<br />

	'''Table 4'''. 1 stage 5 elements CO<sub>3</sub>, HCO<sub>3</sub>, and CO<sub>2</sub> ion mass balance		'''Table 4'''. 1 stage 5 elements CO<sub>3</sub>, HCO<sub>3</sub>, and CO<sub>2</sub> ion mass balance
	[[File:Appendix_3_T4.png\|center\|300px\|]]		[[File:Appendix_3_T4.png\|center\|300px\|]]
			<br />

	'''Table 5'''. 1 stage 1 element CO<sub>3</sub>, HCO<sub>3</sub>, and CO<sub>2</sub> ion mass balance		'''Table 5'''. 1 stage 1 element CO<sub>3</sub>, HCO<sub>3</sub>, and CO<sub>2</sub> ion mass balance
	[[File:Appendix_3_T5.png\|center\|300px\|]]		[[File:Appendix_3_T5.png\|center\|300px\|]]
			<br />

	'''Table 6'''. 2 stages 5,5 elements CO<sub>3</sub>, HCO<sub>3</sub>, and CO<sub>2</sub> ion mass balance		'''Table 6'''. 2 stages 5,5 elements CO<sub>3</sub>, HCO<sub>3</sub>, and CO<sub>2</sub> ion mass balance
	[[File:Appendix_3_T6.png\|center\|300px\|]]		[[File:Appendix_3_T6.png\|center\|300px\|]]
			<br />

	'''Table 7'''. Energy balance on 1 stage 5 elements RO system		'''Table 7'''. Energy balance on 1 stage 5 elements RO system
	[[File:Appendix_3_T7.png\|center\|600px\|frame]]		[[File:Appendix_3_T7.png\|center\|600px\|frame]]
			<br />


	==Appendix 4: Effluent Summary==		==Appendix 4: Effluent Summary==
	[[File:Appendix_4.png\|center]]		[[File:Appendix_4.png\|center]]
			<br />


	==Appendix 5: Cost of Production==		==Appendix 5: Cost of Production==
	[[File:Appendix_5.png\|center]]		[[File:Appendix_5.png\|center]]
			<br />


	==Appendix 6: Economic Anlaysis==		==Appendix 6: Economic Anlaysis==
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	[[File:Appendix_6_C2.png\|center]]		[[File:Appendix_6_C2.png\|center]]
	<br />		<br />


	===Case III: Carlsbad ===		===Case III: Carlsbad ===
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	[[File:Appendix_6_C3.png\|center]]		[[File:Appendix_6_C3.png\|center]]
	<br />		<br />


	===Case IV: Breakeven (NPV = 0 at 10 years)===		===Case IV: Breakeven (NPV = 0 at 10 years)===
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	[[File:Appendix_6_C4.png\|center]]		[[File:Appendix_6_C4.png\|center]]
	<br />		<br />


	===Case V: Breakeven (NPV = 0 at 10 years)===		===Case V: Breakeven (NPV = 0 at 10 years)===
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	[[File:Appendix_6_C5.png\|center]]		[[File:Appendix_6_C5.png\|center]]
	<br />		<br />


	===Case VI: Breakeven (NPV = 0 at 10 years)===		===Case VI: Breakeven (NPV = 0 at 10 years)===

Jstolley: /* Appendices */

2016-03-12T05:47:33Z

Appendices

Bts511: /* Design Basis and Technical Approach */

2016-03-12T03:41:20Z

Design Basis and Technical Approach

← Older revision		Revision as of 03:41, 12 March 2016
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	Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.		Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.

	[[File:Table_1.jpg\|center\|~~800px~~\|~~thumb~~\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]		[[File:Table_1.jpg\|center\|300px\|frame\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]

	=Desalination Overview and Alternatives=		=Desalination Overview and Alternatives=

Bts511: /* Design Basis and Technical Approach */

2016-03-12T03:40:52Z

Design Basis and Technical Approach

← Older revision		Revision as of 03:40, 12 March 2016
Line 47:		Line 47:
	Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.		Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.

	[[File:Table_1.jpg\|center\|800px\|~~frame~~\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]		[[File:Table_1.jpg\|center\|800px\|thumb\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]

	=Desalination Overview and Alternatives=		=Desalination Overview and Alternatives=

Bts511: /* Design Basis and Technical Approach */

2016-03-12T03:40:31Z

Design Basis and Technical Approach

← Older revision		Revision as of 03:40, 12 March 2016
Line 47:		Line 47:
	Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.		Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.

	[[File:Table_1.jpg\|center\|~~400px~~\|frame\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]		[[File:Table_1.jpg\|center\|800px\|frame\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]

	=Desalination Overview and Alternatives=		=Desalination Overview and Alternatives=

Bts511: /* Design Basis and Technical Approach */

2016-03-12T03:39:53Z

Design Basis and Technical Approach

← Older revision		Revision as of 03:39, 12 March 2016
Line 47:		Line 47:
	Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.		Due to the acidity of the desalinated water coming out of the reverse osmosis (RO) system (pH ~ 6), the pumps and pipes carrying the desalinated water for post treatment will likely corrode over time. We have decided to place the desalination plant by the Long Beach Water Reclamation Plant (about 50 meters away) to prevent pipe corrosion.

	[[File:Table_1.jpg\|center\|~~200px~~\|frame\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]		[[File:Table_1.jpg\|center\|400px\|frame\|Table 1. Concentration of the standard seawater, the output from the RO system, and LA standard.]]

	=Desalination Overview and Alternatives=		=Desalination Overview and Alternatives=

Bts511: /* Appendix 7: ROSA Simulation Outputs */

2016-03-12T03:39:13Z

Appendix 7: ROSA Simulation Outputs

← Older revision		Revision as of 03:39, 12 March 2016
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	'''Table 6'''. 2 stage 5,5 elements RO system concentrations and pH in each stream		'''Table 6'''. 2 stage 5,5 elements RO system concentrations and pH in each stream
	[[File:Appendix_7_T6.png\|center\|~~500px~~\|]]		[[File:Appendix_7_T6.png\|center\|700px\|]]

	=References=		=References=
	<references/>		<references/>

Bts511: /* Appendix 7: ROSA Simulation Outputs */

2016-03-12T03:38:25Z

Appendix 7: ROSA Simulation Outputs

← Older revision		Revision as of 03:38, 12 March 2016
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	'''Table 2'''. System detail of 1 stage 1 elements RO system		'''Table 2'''. System detail of 1 stage 1 elements RO system
	[[File:Appendix_7_T2.png\|center]]		[[File:Appendix_7_T2.png\|center\|500px\|]]

	'''Table 3'''. System detail of 2 stage 5,5 elements system		'''Table 3'''. System detail of 2 stage 5,5 elements system
	[[File:Appendix_7_T3.png\|center]]		[[File:Appendix_7_T3.png\|center\|500px\|]]

	'''Table 4'''. 1 stage 5 elements RO system concentrations and pH in each stream		'''Table 4'''. 1 stage 5 elements RO system concentrations and pH in each stream
	[[File:Appendix_7_T4.png\|center]]		[[File:Appendix_7_T4.png\|center\|500px\|]]

	'''Table 5'''. 1 stage 1 element RO system concentration and pH in each stream		'''Table 5'''. 1 stage 1 element RO system concentration and pH in each stream
	[[File:Appendix_7_T5.png\|center]]		[[File:Appendix_7_T5.png\|center\|500px\|]]

	'''Table 6'''. 2 stage 5,5 elements RO system concentrations and pH in each stream		'''Table 6'''. 2 stage 5,5 elements RO system concentrations and pH in each stream
	[[File:Appendix_7_T6.png\|center]]		[[File:Appendix_7_T6.png\|center\|500px\|]]

	=References=		=References=
	<references/>		<references/>

Bts511: /* Appendix 7: ROSA Simulation Outputs */

2016-03-12T03:37:45Z

Appendix 7: ROSA Simulation Outputs

← Older revision		Revision as of 03:37, 12 March 2016
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	'''Table 1'''. System detail of 1 stage 5 elements RO system		'''Table 1'''. System detail of 1 stage 5 elements RO system
	[[File:Appendix_7_T1.png\|center\|\|~~600px~~]]		[[File:Appendix_7_T1.png\|center\|500px\|]]

	'''Table 2'''. System detail of 1 stage 1 elements RO system		'''Table 2'''. System detail of 1 stage 1 elements RO system

← Older revision		Revision as of 05:47, 12 March 2016
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	==Appendix 2: Process Flow Diagram==		==Appendix 2: Process Flow Diagram==
	[[File:Appendix_2.png\|center]]		[[File:Appendix_2.png\|center\|frame]]
	==Appendix 3: Mass and Energy Balance Tables==		==Appendix 3: Mass and Energy Balance Tables==
	'''Table 1'''. Mass balance on 1 stage 5 element RO system, where "out" is the sum of all the concentrate and permeate.		'''Table 1'''. Mass balance on 1 stage 5 element RO system, where "out" is the sum of all the concentrate and permeate.
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	'''Table 7'''. Energy balance on 1 stage 5 elements RO system		'''Table 7'''. Energy balance on 1 stage 5 elements RO system
	[[File:Appendix_3_T7.png\|center\|~~800px~~\|]]		[[File:Appendix_3_T7.png\|center\|600px\|frame]]



	==Appendix 4: Effluent Summary==		==Appendix 4: Effluent Summary==
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	Water is $700; RO with 1 stage and 5 elements		Water is $700; RO with 1 stage and 5 elements
	[[File:Appendix_6_C1.png\|center]]		[[File:Appendix_6_C1.png\|center]]
			<br />

	===Case II===		===Case II===
	Water is $1400; RO with 1 stage and 5 elements		Water is $1400; RO with 1 stage and 5 elements
	[[File:Appendix_6_C2.png\|center]]		[[File:Appendix_6_C2.png\|center]]
			<br />


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	Water is $2257; RO with 1 stage and 5 elements		Water is $2257; RO with 1 stage and 5 elements
	[[File:Appendix_6_C3.png\|center]]		[[File:Appendix_6_C3.png\|center]]
			<br />


	===Case IV: Breakeven (NPV = 0 at 10 years)===		===Case IV: Breakeven (NPV = 0 at 10 years)===
	Water is $2104; RO with 1 stage and 5 elements		Water is $2104; RO with 1 stage and 5 elements
	[[File:Appendix_6_C4.png\|center]]		[[File:Appendix_6_C4.png\|center]]
			<br />


	===Case V: Breakeven (NPV = 0 at 10 years)===		===Case V: Breakeven (NPV = 0 at 10 years)===
	Water is $2112; RO with 2 stages and 5,5 elements		Water is $2112; RO with 2 stages and 5,5 elements
	[[File:Appendix_6_C5.png\|center]]		[[File:Appendix_6_C5.png\|center]]
			<br />


	===Case VI: Breakeven (NPV = 0 at 10 years)===		===Case VI: Breakeven (NPV = 0 at 10 years)===
	Water is $2138 with 1 stage and 1 element		Water is $2138 with 1 stage and 1 element
	[[File:Appendix_6_C6.png\|center]]		[[File:Appendix_6_C6.png\|center]]
			<br />


	==Appendix 7: ROSA Simulation Outputs==		==Appendix 7: ROSA Simulation Outputs==
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	'''Table 1'''. System detail of 1 stage 5 elements RO system		'''Table 1'''. System detail of 1 stage 5 elements RO system
	[[File:Appendix_7_T1.png\|center\|500px\|]]		[[File:Appendix_7_T1.png\|center\|500px\|]]
			<br />

	'''Table 2'''. System detail of 1 stage 1 elements RO system		'''Table 2'''. System detail of 1 stage 1 elements RO system
	[[File:Appendix_7_T2.png\|center\|500px\|]]		[[File:Appendix_7_T2.png\|center\|500px\|]]
			<br />

	'''Table 3'''. System detail of 2 stage 5,5 elements system		'''Table 3'''. System detail of 2 stage 5,5 elements system
	[[File:Appendix_7_T3.png\|center\|500px\|]]		[[File:Appendix_7_T3.png\|center\|500px\|]]
			<br />

	'''Table 4'''. 1 stage 5 elements RO system concentrations and pH in each stream		'''Table 4'''. 1 stage 5 elements RO system concentrations and pH in each stream
	[[File:Appendix_7_T4.png\|center\|500px\|]]		[[File:Appendix_7_T4.png\|center\|500px\|]]
			<br />

	'''Table 5'''. 1 stage 1 element RO system concentration and pH in each stream		'''Table 5'''. 1 stage 1 element RO system concentration and pH in each stream
	[[File:Appendix_7_T5.png\|center\|500px\|]]		[[File:Appendix_7_T5.png\|center\|500px\|]]
			<br />
	'''Table 6'''. 2 stage 5,5 elements RO system concentrations and pH in each stream		'''Table 6'''. 2 stage 5,5 elements RO system concentrations and pH in each stream
	[[File:Appendix_7_T6.png\|center\|700px\|]]		[[File:Appendix_7_T6.png\|center\|700px\|]]