Clifton Star Confirms Excellent Gold Recoveries in Pilot Plant Testing on Duparquet Bulk Sample
18.09.2013 | Marketwired
QUEBEC CITY -- (September 18, 2013) - Clifton Star Resources Inc. ("Clifton Star" or the "Corporation") (TSX VENTURE:CFO) (FRANKFURT:C3T) is pleased to report that it has successfully completed a continuous pilot plant test at SGS Minerals at Lakefield, Ontario, Canada. The tests and analyses were carried out from March to August 2013 to confirm gold recoveries using flotation, pressure oxidation and cyanidation. The tests were highly successful and confirmed earlier bench results.
Highlights: Continuous flotation pilot plant testing was conducted to make a Bulk Concentrate for Pressure Oxidation (POX) pilot testing and also, as an alternate process, to simply produce a High Grade Gold Concentrate that could be sold directly to Smelters.
For the POX process, the Bulk Concentrate produced by flotation assayed 26.8 g/t Au with an average 91.7% gold recovery. After applying POX to the flotation concentrate and cyanide leach to the flotation tailing, the overall average recovery of gold was 92%. Further work has shown that this can reach 94% by using a hot lime treatment of the POX product before cyanidation.
For the Gold Concentrate process, the concentrate assayed an average of 49.9 g/t Au, 50.0 g/t Ag and 31.4% S. Flotation recoveries averaged 86.5% for gold. The flotation tailing was cyanide leached and this raised the overall gold recovery to 91.9%. These concentrates could likely be sold, without further processing to Smelters.
Duparquet Bulk Sample Pilot Tests:
A 12 tonne composite sample of Duparquet mineral sample was prepared by Clifton Star under the supervision of Louis Martin, P.Geo., VP Exploration, and shipped to SGS Minerals. The material was representative of the contribution of the various zones to the Duparquet resource estimate, with a target grade typical of the average grade for the various zones. The pilot plant sample graded 1.835 g/t Au, 2.2 g/t Ag, 1.16 % S and 0.055 % As.
The SGS Pilot Plant was arranged using suitable equipment to simulate a full scale mineral processing plant. The pilot plant received crushed material, which was then continuously ground in a ball mill to approximately 100 micron particle size (P80) and then floated to produce a concentrate enriched in gold and sulfur. The flotation consisted of rougher and cleaner flotation. The flotation of Bulk Concentrate for the POX process required one stage of cleaning. The flotation for the production of the High Grade Gold Concentrate process required two stages of cleaning and an intermediate regrinding step to improve mineral liberation.
The flotation tailings were collected separately from the concentrates. The flotation tailings were tested by cyanidation to determine what additional gold recovery could be obtained. The tailings also underwent environmental characterization and cyanide destruction. Tests for tailing sedimentation were also carried out.
A separate program of testing on crushing and grinding was also carried using a portion of the bulk sample. It included a study of High Pressure Grinding Rolls (HPGR) as part of the comminution strategy. The study will enable Clifton to choose the crushing and grinding parameters best suited for the Duparquet mineralized zones.
For the POX process, the Bulk Concentrate produced assayed 26.8 g/t Au. and flotation recoveries averaged 91.7% Au. After applying POX and cyanide leach to the flotation tailing, the overall recovery of gold was 92%. Further work has shown that this can reach 94% by using a hot lime treatment of the POX product before cyanidation.
For the Gold Concentrate process, the concentrate assayed an average of 49.95 g/t Au, 50.05 g/t Ag and 31.4% S. Flotation recoveries were 86.5% for gold. The flotation tailing was cyanide leached and raised the overall gold recovery to 91.9%. These concentrates could likely be sold, without further processing, to Smelters.
The results confirms prior tests carried out in 2012, and will be incorporated in the ongoing Pre-Feasibility Study on the Duparquet project, due for release in Q1, 2014.
Qualified Person
Dr. David Dreisinger, P.Eng., F.C.I.M., F.C.A.E., is the Qualified Person (NI 43-101) who supervised the preparation of the technical information in this news release. Dr. Dreisinger is Professor and Chairholder, Industrial Research Chair in Hydrometallurgy at the University of British Columbia (Vancouver, Canada) and consults to the worldwide metallurgical industry through Dreisinger Consulting Inc.
Additional Information
All other information previously released on Duparquet is also available on Clifton Star's website at www.cfo-star.com
Neither the TSX Venture Exchange nor its Regulations Services Provider (as the term is defined in policies of the TSX Venture Exchange) accepts responsibility for the adequacy or accuracy of this release.
Cautionary Statement on Forward Looking Information
Certain information included in this press release, including any information as to our future exploration, financial or operating performance and other statements that express management's expectations or estimates of future performance, constitute 'forward-looking statements' within the meaning of the 'safe harbor' provisions of the United States Private Securities Litigation Reform Act of 1995 and Canadian securities laws. The words 'expect', 'believe', 'will', 'intend', 'estimate' and similar expressions identify forward-looking statements. Forward-looking statements are necessarily based upon a number of estimates and assumptions that, while considered reasonable by management, are inherently subject to significant business, economic and competitive uncertainties, risks and contingencies, including the possibility that drill programs will not yield the expected results. The Company cautions the reader that such forward-looking statements involve known and unknown risks, uncertainties and other factors that may cause the actual financial results, performance or achievements of Clifton Star Resources to be materially different from the Company's estimated future results, performance or achievements expressed or implied by those forward-looking statements and that the forward-looking statements are not guarantees of future performance. These statements are also based on certain factors and assumptions. For more details on these estimates, risks, assumptions and factors, see the Company's most recent Form 20-F/Annual Information Form on file with the U.S. Securities and Exchange Commission and Canadian provincial securities regulatory authorities. The Company disclaims any obligation to update or revise any forward-looking statements, whether as a result of new information, events or otherwise, except as expressly required by law. Readers are cautioned not to put undue reliance on these forward-looking statements.
Contact
Clifton Star Resources Inc.
Michel F. Bouchard, President and CEO
mbouchard@cfo-star.com
418-914-9922
www.cfo-star.com / @ cliftonstar1
Highlights: Continuous flotation pilot plant testing was conducted to make a Bulk Concentrate for Pressure Oxidation (POX) pilot testing and also, as an alternate process, to simply produce a High Grade Gold Concentrate that could be sold directly to Smelters.
For the POX process, the Bulk Concentrate produced by flotation assayed 26.8 g/t Au with an average 91.7% gold recovery. After applying POX to the flotation concentrate and cyanide leach to the flotation tailing, the overall average recovery of gold was 92%. Further work has shown that this can reach 94% by using a hot lime treatment of the POX product before cyanidation.
For the Gold Concentrate process, the concentrate assayed an average of 49.9 g/t Au, 50.0 g/t Ag and 31.4% S. Flotation recoveries averaged 86.5% for gold. The flotation tailing was cyanide leached and this raised the overall gold recovery to 91.9%. These concentrates could likely be sold, without further processing to Smelters.
Duparquet Bulk Sample Pilot Tests:
A 12 tonne composite sample of Duparquet mineral sample was prepared by Clifton Star under the supervision of Louis Martin, P.Geo., VP Exploration, and shipped to SGS Minerals. The material was representative of the contribution of the various zones to the Duparquet resource estimate, with a target grade typical of the average grade for the various zones. The pilot plant sample graded 1.835 g/t Au, 2.2 g/t Ag, 1.16 % S and 0.055 % As.
The SGS Pilot Plant was arranged using suitable equipment to simulate a full scale mineral processing plant. The pilot plant received crushed material, which was then continuously ground in a ball mill to approximately 100 micron particle size (P80) and then floated to produce a concentrate enriched in gold and sulfur. The flotation consisted of rougher and cleaner flotation. The flotation of Bulk Concentrate for the POX process required one stage of cleaning. The flotation for the production of the High Grade Gold Concentrate process required two stages of cleaning and an intermediate regrinding step to improve mineral liberation.
The flotation tailings were collected separately from the concentrates. The flotation tailings were tested by cyanidation to determine what additional gold recovery could be obtained. The tailings also underwent environmental characterization and cyanide destruction. Tests for tailing sedimentation were also carried out.
A separate program of testing on crushing and grinding was also carried using a portion of the bulk sample. It included a study of High Pressure Grinding Rolls (HPGR) as part of the comminution strategy. The study will enable Clifton to choose the crushing and grinding parameters best suited for the Duparquet mineralized zones.
For the POX process, the Bulk Concentrate produced assayed 26.8 g/t Au. and flotation recoveries averaged 91.7% Au. After applying POX and cyanide leach to the flotation tailing, the overall recovery of gold was 92%. Further work has shown that this can reach 94% by using a hot lime treatment of the POX product before cyanidation.
For the Gold Concentrate process, the concentrate assayed an average of 49.95 g/t Au, 50.05 g/t Ag and 31.4% S. Flotation recoveries were 86.5% for gold. The flotation tailing was cyanide leached and raised the overall gold recovery to 91.9%. These concentrates could likely be sold, without further processing, to Smelters.
The results confirms prior tests carried out in 2012, and will be incorporated in the ongoing Pre-Feasibility Study on the Duparquet project, due for release in Q1, 2014.
Qualified Person
Dr. David Dreisinger, P.Eng., F.C.I.M., F.C.A.E., is the Qualified Person (NI 43-101) who supervised the preparation of the technical information in this news release. Dr. Dreisinger is Professor and Chairholder, Industrial Research Chair in Hydrometallurgy at the University of British Columbia (Vancouver, Canada) and consults to the worldwide metallurgical industry through Dreisinger Consulting Inc.
Additional Information
All other information previously released on Duparquet is also available on Clifton Star's website at www.cfo-star.com
Neither the TSX Venture Exchange nor its Regulations Services Provider (as the term is defined in policies of the TSX Venture Exchange) accepts responsibility for the adequacy or accuracy of this release.
Cautionary Statement on Forward Looking Information
Certain information included in this press release, including any information as to our future exploration, financial or operating performance and other statements that express management's expectations or estimates of future performance, constitute 'forward-looking statements' within the meaning of the 'safe harbor' provisions of the United States Private Securities Litigation Reform Act of 1995 and Canadian securities laws. The words 'expect', 'believe', 'will', 'intend', 'estimate' and similar expressions identify forward-looking statements. Forward-looking statements are necessarily based upon a number of estimates and assumptions that, while considered reasonable by management, are inherently subject to significant business, economic and competitive uncertainties, risks and contingencies, including the possibility that drill programs will not yield the expected results. The Company cautions the reader that such forward-looking statements involve known and unknown risks, uncertainties and other factors that may cause the actual financial results, performance or achievements of Clifton Star Resources to be materially different from the Company's estimated future results, performance or achievements expressed or implied by those forward-looking statements and that the forward-looking statements are not guarantees of future performance. These statements are also based on certain factors and assumptions. For more details on these estimates, risks, assumptions and factors, see the Company's most recent Form 20-F/Annual Information Form on file with the U.S. Securities and Exchange Commission and Canadian provincial securities regulatory authorities. The Company disclaims any obligation to update or revise any forward-looking statements, whether as a result of new information, events or otherwise, except as expressly required by law. Readers are cautioned not to put undue reliance on these forward-looking statements.
Contact
Clifton Star Resources Inc.
Michel F. Bouchard, President and CEO
mbouchard@cfo-star.com
418-914-9922
www.cfo-star.com / @ cliftonstar1