Light color rosin ester compositions and methods of making same
US-11111411-B2 · Sep 7, 2021 · US
US2021363385A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021363385-A1 |
| Application number | US-202015929780-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 21, 2020 |
| Priority date | May 21, 2020 |
| Publication date | Nov 25, 2021 |
| Grant date | — |
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A process for deodorizing a rosin ester composition is disclosed. The process employs an adsorptive bed containing an adsorbent material. The adsorbent material comprises silica adsorbent having an average pore size between 50-200 Å, BET surface area of at least 300 mm2/g, pore volume of 1.20 to 3.00 cc/g, and a silanol [Si—OH] level of 0.5 to 5 unit/nm2. The deodorized rosin ester composition has an odor intensity reduction of at least 1 unit on odor intensity scale of Offensive Odor Control Act as compared to the rosin ester feedstock. In embodiment, the deodorizing treatment comprises using multi-staged adsorbent system with an adsorbent column having multiple layers of different adsorbent materials.
Opening claim text (preview).
1 . A process for deodorizing a rosin ester composition, the process comprising: providing a rosin ester feedstock in a liquid form having a viscosity in a range of 5-150 cPs, an initial color, and an odor intensity; contacting the rosin ester feedstock with an adsorbent material in an adsorbent bed, obtaining a deodorized rosin ester composition; wherein the adsorbent material comprises silica adsorbent having an average pore size between 50-200 Å, BET surface area of at least 300 mm 2 /g, pore volume of 1.20 to 3.00 cc/g, and a silanol [Si—OH] level of 0.5 to 5 unit/nm 2 ; and wherein the deodorized rosin ester composition has an odor intensity reduction of at least 1 unit on odor intensity scale of Offensive Odor Control Act as compared to the rosin ester feedstock. 2 . The process of claim 1 , wherein the deodorized rosin ester composition has an odor intensity reduction of at least 2 units as compared to the rosin ester feedstock. 3 . The process of claim 2 , wherein the deodorized rosin ester composition has an odor intensity reduction of at least 3 units as compared to the rosin ester feedstock. 4 . The process of claim 1 , wherein the adsorbent bed is operated at an adsorption temperature of 20-30° C., at one bar pressure, and at a superficial velocity (V) of at least 0.3 ft/hr. 5 . The process of claim 4 , wherein the adsorbent bed is operated at a superficial velocity (V) of at least 1 ft/hr. 6 . The process of claim 1 , wherein the deodorized rosin ester composition has a reduction in color of at least 1 Gardner number as compared to the initial color of the rosin ester feedstock. 7 . The process of claim 6 , wherein the deodorized rosin ester composition has a reduction in color of at least 2 Gardner numbers. 8 . The process of claim 1 , wherein providing the rosin ester feedstock in a liquid form comprises dissolving the rosin ester feedstock in a solvent in an amount of 20-70 wt. % rosin ester based on total weight of rosin ester and the solvent. 9 . The process of claim 1 , wherein providing the rosin ester feedstock in a liquid form comprises dissolving the rosin ester feedstock in a solvent in an amount of 30-60 wt. % rosin ester based on total weight of rosin ester and the solvent. 10 . The process of claim 8 , further comprising recovering the deodorized rosin ester by evaporating the solvent. 11 . The process of claim 1 , wherein providing the rosin ester feedstock in a liquid form comprises dissolving the rosin ester feedstock in a solvent selected from alcohols, ethers, ketones, esters, tertiary amides, aliphatic hydrocarbons, aromatic hydrocarbons, and mixtures thereof. 12 . The process of claim 1 , wherein providing the rosin ester feedstock in a liquid form comprises dissolving the rosin ester feedstock in a solvent selected from hexanes, heptanes, petroleum ether, cyclohexane, dipentane, napthal, mineral spirts, toluene, pentane, and mixtures thereof. 13 . The process of claim 1 , further comprising collecting the adsorbent material, and passing a solvent over the adsorbent material in the adsorbent bed, for a sufficient period of time, to dissolve odor causing species and regenerate the adsorbent material. 14 . The process of claim 13 , wherein the solvent used for regenerating the adsorbent material is selected from methanol, ethanol, acetone and mixtures thereof. 15 . The process of claim 1 , wherein the adsorbent bed comprises a multi-stage adsorbent column having at least two layers, each layer with a different adsorbent material. 16 . The process of claim 1 , wherein the adsorbent bed comprises at least two different adsorbent columns, with each adsorbent column containing different adsorbent material. 17 . A deodorized rosin ester composition obtained by the process of claim 1 . 18 . A process for deodorizing a rosin ester composition, the process comprising: providing a rosin ester feedstock in a liquid form having a viscosity in a range of 5-150 cPs; contacting the rosin ester feedstock with two adsorbent beds in series, a first adsorbent bed containing a first adsorbent material and a second adsorbent bed containing a second adsorbent material, obtaining a deodorized rosin ester composition, wherein the first adsorbent material and the second adsorbent material are different, wherein at least one of the first adsorbent material and the second adsorbent material is a silica adsorbent having an average pore size between 50-200 Å, a BET surface area of at least 300 mm 2 /g, pore volume of 1.20 to 3.00 cc/g, and a silanol [Si—OH] level of 0.5 to 5 unit/nm 2 ; and wherein the deodorized rosin ester composition has an odor intensity reduction of at least 2 units on odor intensity scale of Offensive Odor Control Act as compared to the rosin ester feedstock. 19 . The process of claim 18 , wherein the first adsorbent bed and the second adsorbent bed are in a single adsorption column having different layers of adsorbent materials. 20 . A deodorized rosin ester composition obtained by the process of claim 18 .
Use in the form of a bed · CPC title
of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425 · CPC title
in the liquid phase · CPC title
being in the range 2-50 nm, i.e. mesopores · CPC title
being more than 1.0 ml/g · CPC title
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