RDPreheating water jackets

• US 10,112,852 B2
• Filed: 05/10/2017
• Issued: 10/30/2018
• Est. Priority Date: 03/05/2010
• Status: Active Grant

• Current Assignee: RDP Technologies Incorporated
• Original Assignee: RDP Technologies Incorporated
• Inventors: Christy, Richard W., Quici, Michael, Litz, Louis
• Primary Examiner(s): Young, Natasha E
• Application Number:
  US15/591,590
• Publication Number:
  US 20170240441A1
• Time in Patent Office: 538 Days
• CPC Class Codes: C02F 1/008 Control or steering systems not provided for elsewhere in subclass C02F
• CPC Class Codes: C02F 1/529 Processes or devices for preparing lime water
• CPC Class Codes: C02F 1/66 by neutralisation; pH adjustment for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58
• CPC Class Codes: C02F 1/687 Devices for dosing solid compounds
• CPC Class Codes: C02F 2209/005 Processes using a programmable logic controller [PLC]
• CPC Class Codes: C02F 2209/02 Temperature
• CPC Class Codes: C02F 2303/04 Disinfection
• CPC Class Codes: C02F 2303/22 Eliminating or preventing deposits, scale removal, scale prevention C02F1/042, C02F1/4602, C02F5/00 take precedence
• CPC Class Codes: C04B 2/04 Slaking simultaneous dehydrating of gypsum and slaking of lime C04B11/022
• CPC Class Codes: C04B 2/066 Making use of the hydration reaction, e.g. the reaction heat for dehydrating gypsum; Chemical drying by using unslaked lime
• CPC Class Codes: C04B 2/08 Devices therefor

Abstract

Process and apparatus is disclosed for providing a chemical reaction between calcium oxide containing grit particles to produce calcium hydroxide and heat, capturing the heat of hydration and using it to preheat water initially at ambient temperature, to rise to an elevated temperature to increase the amount of lime present in the water to a supersaturated lime suspension level, with the chemical reaction running to completion, followed by cooling. Heat from a water jacket may be used to raise the temperature in the lime slaker. A process and apparatus is also provided for dissolving scale on internal surfaces of a lime slaker, a lime aging tank, grit separation device and piping and dosing sub-systems, by adding acid into the system with rinse water. A pressurized delivery system that is substantially closed to the atmosphere delivers treating doses of slaked lime slurry under sufficient pressure conditions to maintain a relatively constant back pressure, by means of valving.

Claims

1. An apparatus for producing slaked lime slurry comprising:

a programmable control system;

a slaking vessel having at least one support location that is provided with at least one load cell, wherein the load cell provides a load cell signal indicative of a total weight of the slaking vessel and its contents, said load cell communicating with said programmable control system such that said load cell signal can be received by said programmable control system;

slaking vessel temperature sensing means for sensing the temperature of the contents of said slaking vessel, wherein said slaking vessel temperature sensing means provides a slaking vessel temperature signal indicative of the temperature of the contents of said slaking vessel, said slaking vessel temperature sensing means communicating with said programmable control system such that said slaking vessel temperature signal can be received by said programmable control system;

means for charging water into the slaking vessel, said programmable control system communicating with said means for charging water into the slaking vessel, said programmable control system stopping the charging of water into said slaking vessel when said load cell signal indicates that a predetermined weight of water has been charged into said slaking vessel, wherein the water charged into said slaking vessel has a temperature;

means for mixing the content of said slaking vessel;

water temperature control means for controlling the temperature of the water charged into said slaking vessel, said water temperature control means communicating with said programmable control system, said programmable control system controlling said water temperature control means such that the temperature of the water charged into said slaking vessel is within a predetermined water temperature range;

means for charging lime feed stock into the slaking vessel, said programmable control system communicating with said means for charging lime feed stock into the slaking vessel, said programmable control system stopping the charging of lime feed stock into said slaking vessel when said load cell signal indicates that a predetermined weight of lime feed stock has been charged into said slaking vessel, thereby allowing a slaking reaction to take place; and

means for discharging the contents of said slaking vessel;

said programmable control system communicating with said means for discharging the contents of said slaking vessel, said programmable control system monitoring the temperature of the contents of said slaking vessel using said slaking vessel temperature signal, said programmable control system operating said means for discharging the contents of said slaking vessel to discharge the contents of said slaking vessel when the temperature of the contents of said slaking vessel remains within a predetermined temperature range for a predetermined period of time.

2. The apparatus according to claim 1, wherein said programmable control system controls the temperature of the water charged into said slaking vessel such that the contents of said slaking vessel will be at a temperature in the range of 180°

F. to 195°

F. at least when the slaking reaction substantially reaches completion, said programmable control system determining the temperature range for the water to be charged to said slaking vessel using at least the predetermined weight of the water to be charged to said slaking vessel and the predetermined weight of the lime feed stock to be charged to said slaking vessel, wherein said programmable control system operates said water temperature control means such that the water temperature of the water charged to said slaking vessel is initially within the water temperature range determined by said a logic means before the lime feed stock is charged to the slaking vessel.

3. The apparatus according to claim 2, wherein said water temperature control means comprises a heater supplied with energy from an auxiliary energy source.

4. The apparatus according to claim 3, wherein the slaking reaction generates heat, wherein said slaking vessel has a jacket surrounding an inner compartment where the contents of the slaking vessel are held at least during the slaking reaction, and wherein said water temperature control means further comprises:

piping and one or more valves controlled by said programmable control system to direct at least a portion of the water to be charged to said slaking vessel into and out of said jacket to thereby recover at least a part of the heat generated by the slaking reaction and at least reduce the energy required for heating water by said heater;

piping for directing water from said jacket to said heater;

piping and valves for directing one of water from a process water supply source, water from said heater, and a mixture thereof to said slaking vessel.

5. The apparatus according to claim 4, wherein the contents of said slaking vessel after the slaking reaction substantially reaches completion is in the form of a slaked lime slurry, wherein the slurry aging tank has a jacket surrounding an inner compartment where the slaked lime slurry is stored, and wherein the at least a portion of the water to be charged to said slaking vessel is directed into and out of said jacket of said slurry aging tank before it is directed into said jacket of said slaking vessel.