Continuous process for drying microcapsules
The invention teaches continuous process for rapidly drying a population of pressure sensitive microcapsules. The process comprises the steps of a) preparing a slurry comprising pressure-sensitive microcapsules dispersed in an aqueous carrier solution and encapsulating a non-solid core material; b) providing a pulse combustor having a means for generating a pulsating flow of hot gases, the pulse combustor having an associated combustion chamber with inlet means for introducing fuel and combustion air to the combustion chamber whereby the combination of the pulse combustor and the combustion chamber generate a pulsating flow of hot gases, the pulse combustor having an outlet means for discharging the pulsating flow of hot gases, and a material feed introduction chamber connected proximate the outlet means of the combustion chamber; c) inputting the slurry of microcapsules into the material feed introduction chamber; d) converting the slurry of microcapsules to dried microcapsules in a drying chamber communicating with the combustion chamber through the outlet means, the drying chamber receiving the microcapsule slurry fed into the material feed introduction chamber and the pulsating flow of hot gases; and, e) collecting in a collection assembly associated with the drying chamber the microcapsules dried in the drying chamber, whereby the collected microcapsules are substantially free of breakage.
1 . A continuous process for rapidly drying a population of pressure sensitive microcapsules, said process comprising:
a) preparing a slurry material comprising pressure-sensitive microcapsules dispersed in an aqueous carrier solution and encapsulating a non-solid core material;
b) providing a pulse combustor having a means for generating a pulsating flow of hot gases, the pulse combustor having an associated combustion chamber with inlet means for introducing fuel and combustion air to the combustion chamber whereby the combination of the pulse combustor and the combustion chamber generate a pulsating flow of hot gases, the pulse combustor having an outlet means for discharging the pulsating flow of hot gases, and a material feed introduction chamber connected proximate the outlet means of the combustion chamber;
c) inputting the slurry of microcapsules into the material feed introduction chamber;
d) converting the slurry of microcapsules to dried microcapsules in a drying chamber communicating with the combustion chamber through the outlet means, the drying chamber receiving the microcapsule slurry fed into the material feed introduction chamber and the pulsating flow of hot gases;
e) collecting in a collection assembly associated with the drying chamber the microcapsules dried in the drying chamber, whereby the collected microcapsules are separated substantially free of breakage.
2 . The process according to claim 1 wherein the process wherein the combustion air at the outlet means is at a temperature of at least 77° C.
3 . The process according to claim 1 wherein the air is injected into the pulse combustor at a pressure of at least 30 psi.
4 . The process according to claim 1 wherein, the microcapsule slurry is input into the reactor at a slurry concentration of from 1 to 65% solids.
5 . The process according to claim 1 wherein the residence time of the slurry in the drying chamber is selected sufficient to dry the slurry material.
6 . The process according to claim 1 wherein the microcapsules are dried to a moisture content of from 0 to 14%.
7 . A continuous process for rapidly drying a population of pressure sensitive microcapsules, said process comprising:
a) preparing a slurry material comprising pressure-sensitive microcapsules dispersed in an aqueous carrier solution and encapsulating a non-solid core material;
b) providing a pulse combustor having a means for generating a pulsating flow of hot gases, the pulse combustor having an associated combustion chamber with inlet means for introducing fuel and combustion air to the combustion chamber whereby the combination of the pulse combustor and the combustion chamber generate a pulsating flow of hot gases, the pulse combustor having an outlet means for discharging the pulsating flow of hot gases, and a material feed introduction chamber connected proximate the outlet means of the combustion chamber;
c) inputting the slurry of microcapsules into the material feed introduction chamber;
d) converting the slurry of microcapsules to dried microcapsules in a drying chamber communicating with the combustion chamber through the outlet means, the drying chamber receiving the microcapsule slurry fed into the material feed introduction chamber and the pulsating flow of hot gases;
e) collecting in a collection assembly associated with the drying chamber the microcapsules dried in the drying chamber;
f) separating the dried microcapsules with separator means provided for separating the flow of hot gases from the dried microcapsules exiting the drying chamber, whereby the dried microcapsules are separated substantially free of breakage.
8 . The process according to claim 7 wherein the combustion air at the outlet means is at a temperature of at least 77° C.
9 . The process according to claim 7 wherein the microcapsule slurry is input into the reactor at a rate of from 1 to 65% solids.
10 . The process according to claim 7 wherein the residence time of the slurry in the drying chamber is sufficient to dry the slurry material such that the exit temperature of the gases at the outlet means is from 60° C. to 130° C.
11 . The process according to claim 7 wherein the microcapsules are dried to a moisture content of from 0 to 8%.