Direct flow crystal growth system
Abstract
This patent describes a method of growing a crystal having increased damage threshold, in a crystal growth tank filled with crystal growing solution. It comprises maintaining the solution in the tank at substantially its saturation temperature; continuously removing solution from the tank; heating the solution removed from the tank to a predetermined temperature above the saturation temperature; filtering the heated solution through a 0.5 micron filter; cooling the filtered heated solution to substantially its saturation temperature; continuously returning the cooled filtered solution to the tank; wherein the steps of removing, filtering, cooling and returning are performed in a continuous flow system.
- Inventors:
- Publication Date:
- OSTI Identifier:
- 7252372
- Patent Number(s):
- US 5122224; A
- Application Number:
- PPN: US 7-428538; TRN: 92-031396
- Assignee:
- US Dept. of Energy, Washington, DC (United States)
- Resource Type:
- Patent
- Resource Relation:
- Patent File Date: 30 Oct 1989
- Country of Publication:
- United States
- Language:
- English
- Subject:
- 75 CONDENSED MATTER PHYSICS, SUPERCONDUCTIVITY AND SUPERFLUIDITY; SOLID SOLUTIONS; CRYSTAL GROWTH METHODS; COOLING; FILTRATION; HEAT TREATMENTS; PROCESS CONTROL; TANKS; CONTAINERS; CONTROL; DISPERSIONS; MIXTURES; SEPARATION PROCESSES; SOLUTIONS; 665300* - Interactions Between Beams & Condensed Matter- (1992-)
Citation Formats
Montgomery, K E, and Milanovich, F P. Direct flow crystal growth system. United States: N. p., 1992.
Web.
Montgomery, K E, & Milanovich, F P. Direct flow crystal growth system. United States.
Montgomery, K E, and Milanovich, F P. 1992.
"Direct flow crystal growth system". United States.
@article{osti_7252372,
title = {Direct flow crystal growth system},
author = {Montgomery, K E and Milanovich, F P},
abstractNote = {This patent describes a method of growing a crystal having increased damage threshold, in a crystal growth tank filled with crystal growing solution. It comprises maintaining the solution in the tank at substantially its saturation temperature; continuously removing solution from the tank; heating the solution removed from the tank to a predetermined temperature above the saturation temperature; filtering the heated solution through a 0.5 micron filter; cooling the filtered heated solution to substantially its saturation temperature; continuously returning the cooled filtered solution to the tank; wherein the steps of removing, filtering, cooling and returning are performed in a continuous flow system.},
doi = {},
url = {https://www.osti.gov/biblio/7252372},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Tue Jun 16 00:00:00 EDT 1992},
month = {Tue Jun 16 00:00:00 EDT 1992}
}
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