Abstract Wastewaters, from a coke oven by-product plant, containing cyanides and objectionable complex organic compounds are treated by a high density sludge process. The wastewaters are mixed with an aqueous high calcium lime slurry and a portion of the sludge formed in the process, which portion is recycled in the process. The aqueous high calcium lime slurry and the portion of recycled sludge are mixed for a time to obtain a uniform mix. A solution containing iron values is added to the uniform mix. Iron cyanide compounds and a portion of the complex organic compounds are precipitated. The precipitate is flocculated and is passed to a settling tank wherein the precipitate settles out to form a high density sludge.
A PROCESS FOR REMOVING CYANIDES AND COMPLES ORGANIC COMPOUNDS WHICH COLOR LIQUID WASTES FROM COKE OVEN WASTEWATERS, COMPRISING: A. MIXING HIGH CALCIUM LIME, THE WASTEWATER TO BE PURIFIED AND A MAJRO PORTION OF THE HIGH DENSITY SLUDGE FORMED IN STEP (E) IN A FIRST REACTOR FORMING A FIRST MIX HAVING A PH OF BETWEEN ABOUT 10.0 TO ABOUT 12.0, B. TRANSFERRING THE FIRST MIX FROM THE SAID FIRST REACTOR TO A SECOND REACTOR, C. MIXING A SOLUTION SELECTED FROM THE GROUP CONSISTING OF ACID MINE DRAINAGE AND WASTE PICKLE LIQUOR, WHICH SOLUTION CONTAINS IRON VALUES INTO THE FIRST MIX IN THE SECOND REACTOR TO FORM A SECOND MIX HAVING A PH OF BETWEEN ABOUT 9.0 TO ABOUT 10.0 AND PRECIPITATING A MAJOR PORTION OF THE CYANIDES AND COMPLEX ORGANIC COMPOUNDS ORIGINALLY PRESENT IN THE WASTEWATER BEING PURIFIED. D. FLOCCULATING THE PRECIPITATE FORMED IN STEP (C). E. PASSING THE SECOND MIX CONTAINING FLOCCULATED PRECIPITATE OF STEP (D) TO A SETTLING MEANS WHEREIN THE FLOCCULATED PRECIPITATE SETTLES OUT AS A HIGH DENSITY SLUDGE AND CLARIFIED WATER IS DECANTED FROM THE SETTLING MEANS, AND F. RECYCLING BACK TO THE FIRST REACTOR FROM ABOUT 20 POUNDS TO 40 POUNDS OF THE HIGH DENSITY SLUDGE FORMED IN STEP (E) FOR EVERY POUND OF NEW PRECIPITATE FORMED IN STEP (C).
Claim 2
Dependent Claim
214 words
A PROCESS FOR REMOVING CYANIDES AND COMPLES ORGANIC COMPOUNDS WHICH COLOR LIQUID WASTES FROM COKE OVEN WASTEWATERS, COMPRISING: A. MIXING HIGH CALCIUM LIME, THE WASTEWATER TO BE PURIFIED AND A MAJRO PORTION OF THE HIGH DENSITY SLUDGE FORMED IN STEP (E) IN A FIRST REACTOR FORMING A FIRST MIX HAVING A PH OF BETWEEN ABOUT 10.0 TO ABOUT 12.0, B. TRANSFERRING THE FIRST MIX FROM THE SAID FIRST REACTOR TO A SECOND REACTOR, C. MIXING A SOLUTION SELECTED FROM THE GROUP CONSISTING OF ACID MINE DRAINAGE AND WASTE PICKLE LIQUOR, WHICH SOLUTION CONTAINS IRON VALUES INTO THE FIRST MIX IN THE SECOND REACTOR TO FORM A SECOND MIX HAVING A PH OF BETWEEN ABOUT 9.0 TO ABOUT 10.0 AND PRECIPITATING A MAJOR PORTION OF THE CYANIDES AND COMPLEX ORGANIC COMPOUNDS ORIGINALLY PRESENT IN THE WASTEWATER BEING PURIFIED. D. FLOCCULATING THE PRECIPITATE FORMED IN STEP (C). E. PASSING THE SECOND MIX CONTAINING FLOCCULATED PRECIPITATE OF STEP (D) TO A SETTLING MEANS WHEREIN THE FLOCCULATED PRECIPITATE SETTLES OUT AS A HIGH DENSITY SLUDGE AND CLARIFIED WATER IS DECANTED FROM THE SETTLING MEANS, AND F. RECYCLING BACK TO THE FIRST REACTOR FROM ABOUT 20 POUNDS TO 40 POUNDS OF THE HIGH DENSITY SLUDGE FORMED IN STEP (E) FOR EVERY POUND OF NEW PRECIPITATE FORMED IN STEP (C).
Claim 3
Dependent Claim
20 words
The process of claim 1 in which the solution containing iron values added in step (c) is acid mine drainage.
Claim 4
Dependent Claim
20 words
The process of claim 1 in which the solution containing iron values added in step (c) is waste pickle liquor.