<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-09-20T10:21:16Z</responseDate><request verb="GetRecord" identifier="oai:dspace.mit.edu:1721.1/70402" metadataPrefix="dim">https://dspace.mit.edu/server/oai/request</request><GetRecord><record><header><identifier>oai:dspace.mit.edu:1721.1/70402</identifier><datestamp>2022-01-13T07:54:19Z</datestamp><setSpec>com_1721.1_7582</setSpec><setSpec>com_1721.1_7581</setSpec><setSpec>col_1721.1_131022</setSpec></header><metadata><dim:dim xmlns:dim="http://www.dspace.org/xmlns/dspace/dim" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:doc="http://www.lyncode.com/xoai" xsi:schemaLocation="http://www.dspace.org/xmlns/dspace/dim http://www.dspace.org/schema/dim.xsd">
   <dim:field mdschema="dc" element="contributor" qualifier="advisor" lang="en_US">Jefferson W. Tester.</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="author" lang="en_US">Johnson, Michael C., Ph. D. Massachusetts Institute of Technology</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="other" lang="en_US">Massachusetts Institute of Technology. Dept. of Chemical Engineering.</dim:field>
   <dim:field mdschema="dc" element="contributor" qualifier="department">Massachusetts Institute of Technology. Department of Chemical Engineering</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="accessioned">2012-04-26T18:50:08Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="available">2012-04-26T18:50:08Z</dim:field>
   <dim:field mdschema="dc" element="date" qualifier="issued" lang="en_US">2012</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="uri">http://hdl.handle.net/1721.1/70402</dim:field>
   <dim:field mdschema="dc" element="identifier" qualifier="oclc" lang="en_US">784099822</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2012.</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">"February 2012." Cataloged from PDF version of thesis.</dim:field>
   <dim:field mdschema="dc" element="description" lang="en_US">Includes bibliographical references.</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="abstract" lang="en_US">High-lipid algae are potential sources of biofuels. Lipids in this biomass provide a straightforward chemical route to hydrocarbon-based high energy-density fuels needed for diesel and jet engines. However, current schemes for producing these biofuels require large amounts of energy and solvents to recover the oil. The feedstocks have dilute concentrations (1 wt% or less) in aqueous media, and must be dewatered significantly to form biofuels. A hydrothermal environment, utilizing a highpressure, high-temperature, water-based medium, is well-suited for processing these dilute biomass feedstocks. Conversion of high-lipid model feedstocks to bio-crude oils was investigated over temperatures from 250 to 350 C and a wide range of reaction times (from minutes to several hours). Temperature and pressure controlled batch reactions were performed on Isochrysis sp., and T. Weissflogii. Chemical analysis was performed to give a detailed characterization of the products, including fatty acid conversion and oil yields. Product analysis was thorough enough to be used for simulation of the hydrothermal process. These results were used to fit a model for lipid reactions in hydrothermal systems. Life cycle assessment (LCA) of the algal hydrothermal process was performed for comparison to conventional algal biofuel production techniques. Extraction and conversion to fuels had similar energy inputs for either hydrothermal or extracted oil.</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="statementofresponsibility" lang="en_US">by Michael C. Johnson.</dim:field>
   <dim:field mdschema="dc" element="description" qualifier="degree" lang="en_US">Ph.D.</dim:field>
   <dim:field mdschema="dc" element="format" qualifier="extent" lang="en_US">187 p.</dim:field>
   <dim:field mdschema="dc" element="language" qualifier="iso" lang="en_US">eng</dim:field>
   <dim:field mdschema="dc" element="publisher" lang="en_US">Massachusetts Institute of Technology</dim:field>
   <dim:field mdschema="dc" element="rights" lang="en_US">M.I.T. theses are protected by 
copyright. They may be viewed from this source for any purpose, but 
reproduction or distribution in any format is prohibited without written 
permission. See provided URL for inquiries about permission.</dim:field>
   <dim:field mdschema="dc" element="rights" qualifier="uri" lang="en_US">http://dspace.mit.edu/handle/1721.1/7582</dim:field>
   <dim:field mdschema="dc" element="subject" lang="en_US">Chemical Engineering.</dim:field>
   <dim:field mdschema="dc" element="title" lang="en_US">Hydrothermal processing of high-lipid biomass to fuels</dim:field>
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   	&lt;Title>Hydrothermal processing of high-lipid biomass to fuels&lt;/Title>
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   	&lt;PublicationDate>2012&lt;/PublicationDate>
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        	&lt;DisplayName>Johnson, Michael C., Ph. D. Massachusetts Institute of Technology&lt;/DisplayName>
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    &lt;Keyword>Chemical Engineering.&lt;/Keyword>
   	&lt;Abstract>High-lipid algae are potential sources of biofuels. Lipids in this biomass provide a straightforward chemical route to hydrocarbon-based high energy-density fuels needed for diesel and jet engines. However, current schemes for producing these biofuels require large amounts of energy and solvents to recover the oil. The feedstocks have dilute concentrations (1 wt% or less) in aqueous media, and must be dewatered significantly to form biofuels. A hydrothermal environment, utilizing a highpressure, high-temperature, water-based medium, is well-suited for processing these dilute biomass feedstocks. Conversion of high-lipid model feedstocks to bio-crude oils was investigated over temperatures from 250 to 350 C and a wide range of reaction times (from minutes to several hours). Temperature and pressure controlled batch reactions were performed on Isochrysis sp., and T. Weissflogii. Chemical analysis was performed to give a detailed characterization of the products, including fatty acid conversion and oil yields. Product analysis was thorough enough to be used for simulation of the hydrothermal process. These results were used to fit a model for lipid reactions in hydrothermal systems. Life cycle assessment (LCA) of the algal hydrothermal process was performed for comparison to conventional algal biofuel production techniques. Extraction and conversion to fuels had similar energy inputs for either hydrothermal or extracted oil.&lt;/Abstract>
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