Gerard Hofland | Delft University of Technology (original) (raw)
Papers by Gerard Hofland
Journal of Chromatography B: Biomedical Sciences and Applications, 2000
International Journal of Pharmaceutics, 2008
Pharmaceutical Research, 2004
The Journal of Supercritical Fluids, 2011
The Journal of Supercritical Fluids, 2008
The Journal of Supercritical Fluids, 2008
Journal of Chemical & Engineering Data, 2007
ABSTRACT The solubilities of α-, β-, and γ-glycine in aqueous solutions containing methanol, etha... more ABSTRACT The solubilities of α-, β-, and γ-glycine in aqueous solutions containing methanol, ethanol, 2-propanol, or acetone were measured at 310 K. The solubility of all the polymorphs dropped rapidly as a function of the concentration of antisolvent. The solubility of the glycine polymorphs in water−antisolvent mixtures was, in decreasing order: methanol > ethanol > 2-propanol > acetone. The solubility of α-glycine was slightly higher than that of γ-glycine, but the solubility of β-glycine was significantly higher by up to 17 %. The induction time for the recrystallization of β- to α-glycine in those water−antisolvent mixtures was, in decreasing order: methanol > ethanol > acetone > 2-propanol. This signifies that the selection of an antisolvent for preparation of β-glycine can have an important effect on the product.
Journal of Chemical & Engineering Data, 2007
Journal of Agricultural and Food Chemistry, 2009
Mixtures of fatty acid ethyl esters were produced by lipase-catalyzed ethanolysis of milk fat tri... more Mixtures of fatty acid ethyl esters were produced by lipase-catalyzed ethanolysis of milk fat triglycerides. Three commercial immobilized lipases (Lipozyme TL, Lipozyme RM, and Novozym 435) were tested in different reaction conditions with the aim of maximizing the conversion of the short-chain fatty acid fraction of milk fat to flavor ethyl esters. The influence of the reactants molar ratio was investigated, as well as three different reaction media, that is, hexane, CO(2)-expanded liquid (GXL), and the solvent-free mixture. Novozym 435 showed the highest activity in all conditions. This lipase also exhibited selectivity for short-chain fatty acids, which, at short reaction times, resulted in a product mixture richer in short-chain fatty acids than the original milk fat. The highest selectivities were obtained in hexane and in CO(2)-expanded liquid fat, at low ethanol to fat ratios. Using dense CO(2) as the reaction cosolvent is attractive because it results in the largest short-chain fatty acid enrichment in the product mixture, while leaving no residues in the product.
Industrial & Engineering Chemistry Research, 1999
ABSTRACT High-pressure CO2 was used as a recyclable acid for the isoelectric precipitation of cas... more ABSTRACT High-pressure CO2 was used as a recyclable acid for the isoelectric precipitation of casein. Measurement of the pH during the high-pressure process allowed the comparison of the process with conventional precipitation using sulfuric acid. A simple model was made up to calculate the pH in complex aqueous solutions pressurized with CO2. It was established that the isoelectric point (pH 4.6) could not be reached with CO2, unless the milk was diluted. Nevertheless, high precipitation yields could be obtained with this process. Still, it was found that the precipitation is mainly caused by the decrease in pH. The removal of calcium phosphate appeared to be complicated, probably because of precipitation of calcium phosphate in the casein-free solutions after the pressure is released.
European Journal of Pharmaceutics and Biopharmaceutics, 2008
European Journal of Pharmaceutical Sciences, 2006
European Journal of Lipid Science and Technology, 2011
ABSTRACT We propose a novel process for the production of a DAG-rich acylglycerol mixture derived... more ABSTRACT We propose a novel process for the production of a DAG-rich acylglycerol mixture derived from milk fat. This product has potentially interesting nutritional properties, derived from both its high content of DAG and of short-chain fatty acids (FAs). The proposed process consists of three steps: lipase-catalysed partial ethanolysis of milk fat, extraction of the by-product fatty acid ethyl esters (FAEEs) using supercritical carbon dioxide (SC-CO2) and isomerization of DAG to increase the proportion of 1,3-DAG. The experimental investigation of the process steps was done using milk fat and trilaurin. Several lipases were tested for maximizing the percentage of DAG in the acylglycerol mixture produced by ethanolysis. The selectivity of the chosen lipase was such that the produced AG mixture was enriched in short-chain FAs in relation to the original milk fat. FAEEs were completely extracted from the ethanolysis mixture by SC-CO2. In the final process step, we explored the reaction conditions for facilitating acyl migration in the DAG mixture, so that the equilibrium proportion of 1,3-DAG (∼64%) was attained. Our results set the basis for the development of a simple process for the production of a DAG-rich milk fat analogue.
European Food Research and Technology, 2011
Crystal Growth & Design, 2007
The precipitation of amino acids and mannitol from aqueous solution was studied in a spraying pro... more The precipitation of amino acids and mannitol from aqueous solution was studied in a spraying process using a mixture of supercritical CO2 and ethanol as drying medium and as anti-solvent. By changing the flow rates, the process was tuned to selectively precipitate α- ...
Biotechnology Progress, 2001
Biotechnology and Bioengineering, 2001
Fractionation of specific proteins from plant material is a complex and involved science, yet pur... more Fractionation of specific proteins from plant material is a complex and involved science, yet pure protein extracts are in high demand by a wide range of food and pharmaceutical industries. In this study carbon dioxide has been used as a volatile electrolyte to isoelectrically precipitate two major protein constituents of soybean. Carbon dioxide was shown to be effective in purifying glycinin and beta-conglycinin in a three-step process as 95% and 80% concentrated fractions with precipitation yields of 28% and 21%, respectively. Recycling of the mixed precipitate of the intermediary step enables complete separation into the concentrated fractions. Fractionation acidity was precisely controlled by a simple modification of pressure. In addition, the occurrence of a pH overshoot was prevented at any point in the fractionation vessel, as the pH minimum was defined by its equilibrium relationship with carbon dioxide operating pressure. The removal of the glycinin precipitate was an important factor in the purification procedure. The yield of the individual concentrated glycinin and beta-conglycinin precipitate fractions was a function of carbon dioxide pressure, extract concentration and, to a much lesser extent, temperature.
Journal of Chromatography B: Biomedical Sciences and Applications, 2000
International Journal of Pharmaceutics, 2008
Pharmaceutical Research, 2004
The Journal of Supercritical Fluids, 2011
The Journal of Supercritical Fluids, 2008
The Journal of Supercritical Fluids, 2008
Journal of Chemical & Engineering Data, 2007
ABSTRACT The solubilities of α-, β-, and γ-glycine in aqueous solutions containing methanol, etha... more ABSTRACT The solubilities of α-, β-, and γ-glycine in aqueous solutions containing methanol, ethanol, 2-propanol, or acetone were measured at 310 K. The solubility of all the polymorphs dropped rapidly as a function of the concentration of antisolvent. The solubility of the glycine polymorphs in water−antisolvent mixtures was, in decreasing order: methanol > ethanol > 2-propanol > acetone. The solubility of α-glycine was slightly higher than that of γ-glycine, but the solubility of β-glycine was significantly higher by up to 17 %. The induction time for the recrystallization of β- to α-glycine in those water−antisolvent mixtures was, in decreasing order: methanol > ethanol > acetone > 2-propanol. This signifies that the selection of an antisolvent for preparation of β-glycine can have an important effect on the product.
Journal of Chemical & Engineering Data, 2007
Journal of Agricultural and Food Chemistry, 2009
Mixtures of fatty acid ethyl esters were produced by lipase-catalyzed ethanolysis of milk fat tri... more Mixtures of fatty acid ethyl esters were produced by lipase-catalyzed ethanolysis of milk fat triglycerides. Three commercial immobilized lipases (Lipozyme TL, Lipozyme RM, and Novozym 435) were tested in different reaction conditions with the aim of maximizing the conversion of the short-chain fatty acid fraction of milk fat to flavor ethyl esters. The influence of the reactants molar ratio was investigated, as well as three different reaction media, that is, hexane, CO(2)-expanded liquid (GXL), and the solvent-free mixture. Novozym 435 showed the highest activity in all conditions. This lipase also exhibited selectivity for short-chain fatty acids, which, at short reaction times, resulted in a product mixture richer in short-chain fatty acids than the original milk fat. The highest selectivities were obtained in hexane and in CO(2)-expanded liquid fat, at low ethanol to fat ratios. Using dense CO(2) as the reaction cosolvent is attractive because it results in the largest short-chain fatty acid enrichment in the product mixture, while leaving no residues in the product.
Industrial & Engineering Chemistry Research, 1999
ABSTRACT High-pressure CO2 was used as a recyclable acid for the isoelectric precipitation of cas... more ABSTRACT High-pressure CO2 was used as a recyclable acid for the isoelectric precipitation of casein. Measurement of the pH during the high-pressure process allowed the comparison of the process with conventional precipitation using sulfuric acid. A simple model was made up to calculate the pH in complex aqueous solutions pressurized with CO2. It was established that the isoelectric point (pH 4.6) could not be reached with CO2, unless the milk was diluted. Nevertheless, high precipitation yields could be obtained with this process. Still, it was found that the precipitation is mainly caused by the decrease in pH. The removal of calcium phosphate appeared to be complicated, probably because of precipitation of calcium phosphate in the casein-free solutions after the pressure is released.
European Journal of Pharmaceutics and Biopharmaceutics, 2008
European Journal of Pharmaceutical Sciences, 2006
European Journal of Lipid Science and Technology, 2011
ABSTRACT We propose a novel process for the production of a DAG-rich acylglycerol mixture derived... more ABSTRACT We propose a novel process for the production of a DAG-rich acylglycerol mixture derived from milk fat. This product has potentially interesting nutritional properties, derived from both its high content of DAG and of short-chain fatty acids (FAs). The proposed process consists of three steps: lipase-catalysed partial ethanolysis of milk fat, extraction of the by-product fatty acid ethyl esters (FAEEs) using supercritical carbon dioxide (SC-CO2) and isomerization of DAG to increase the proportion of 1,3-DAG. The experimental investigation of the process steps was done using milk fat and trilaurin. Several lipases were tested for maximizing the percentage of DAG in the acylglycerol mixture produced by ethanolysis. The selectivity of the chosen lipase was such that the produced AG mixture was enriched in short-chain FAs in relation to the original milk fat. FAEEs were completely extracted from the ethanolysis mixture by SC-CO2. In the final process step, we explored the reaction conditions for facilitating acyl migration in the DAG mixture, so that the equilibrium proportion of 1,3-DAG (∼64%) was attained. Our results set the basis for the development of a simple process for the production of a DAG-rich milk fat analogue.
European Food Research and Technology, 2011
Crystal Growth & Design, 2007
The precipitation of amino acids and mannitol from aqueous solution was studied in a spraying pro... more The precipitation of amino acids and mannitol from aqueous solution was studied in a spraying process using a mixture of supercritical CO2 and ethanol as drying medium and as anti-solvent. By changing the flow rates, the process was tuned to selectively precipitate α- ...
Biotechnology Progress, 2001
Biotechnology and Bioengineering, 2001
Fractionation of specific proteins from plant material is a complex and involved science, yet pur... more Fractionation of specific proteins from plant material is a complex and involved science, yet pure protein extracts are in high demand by a wide range of food and pharmaceutical industries. In this study carbon dioxide has been used as a volatile electrolyte to isoelectrically precipitate two major protein constituents of soybean. Carbon dioxide was shown to be effective in purifying glycinin and beta-conglycinin in a three-step process as 95% and 80% concentrated fractions with precipitation yields of 28% and 21%, respectively. Recycling of the mixed precipitate of the intermediary step enables complete separation into the concentrated fractions. Fractionation acidity was precisely controlled by a simple modification of pressure. In addition, the occurrence of a pH overshoot was prevented at any point in the fractionation vessel, as the pH minimum was defined by its equilibrium relationship with carbon dioxide operating pressure. The removal of the glycinin precipitate was an important factor in the purification procedure. The yield of the individual concentrated glycinin and beta-conglycinin precipitate fractions was a function of carbon dioxide pressure, extract concentration and, to a much lesser extent, temperature.