Process for recovering methylene chloride
AssigneeXerox Corporation
InventorsThomas B. Glenwright, Warren R. Smith, Betsy B. Dodge, Steven P. Wazenkewitz, Ronald L. Swift
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Abstract
A system for recovering methylene chloride from an aqueous waste stream is disclosed. The system includes a distillation unit, at least one heat transfer unit, receptacles for methylene chloride and waste product, a temperature probe and a controller configured to selectively divert product flow from the distillation unit to either of the receptacles or to a recycle line back to the distillation unit depending upon the temperature measured by the probe. Also disclosed is a related process of recovering methylene chloride with such a system.
Claims3
A process for improving the reclaim efficiency of methylene chloride from a mixture including water and methylene chloride, said process comprising:
- providing a system including (i) a distillation unit having an inlet and an outlet, (ii) a plurality of selectively positionable control valves, each having an inlet and an outlet, one of said outlets being in communication with said inlet of said distillation unit, (iii) a plurality of temperature sensors and means for providing a control signal corresponding to sensed temperatures, and (iv) a controller in communication with said temperature sensors and said control valves;
- directing said mixture including water and methylene chloride to said inlet of said distillation unit;
- operating said distillation unit to produce a product stream at said outlet of said distillation unit;
- measuring the temperature of said product stream and at a lower region of said distillation unit with said temperature sensors;
- providing said control signal from said temperature sensors to said controller;
- operating said controller to selectively position said control valves based upon said control signal;
- whereby upon measuring the temperature of said product stream to be greater than 1.05° F. and the temperature at said lower region of said distillation unit to be greater than or equal to 104.5° F., said controller positions said control valves to direct said product stream to said inlet of said distillation unit.
Dependencies are inferred from the claim text.