【正文】 Method for processing goldbearing sulfide ores involving preparation of a sulfide concentrate. United States Patent. November 17, 1998. [12] Kleid, etal. Processes to recover and reconcentrate gold from its ores. United States Patent. January 3, 1995.致謝！設(shè)備附表附表1 顎式破碎機類型復(fù)擺破碎機型號與規(guī)格PE7501060進(jìn)料口（長寬）/mm10607500最大給礦粒度/mm630處理量/m3/h70～130排礦口范圍/mm80～140主軸轉(zhuǎn)速/rmin1250傳動電動機功率/KW110質(zhì)量/t28附表2 PYB1200/170標(biāo)準(zhǔn)圓錐破碎機破碎機總重/t破碎機直徑/mm1200給料口尺寸/mm170給料尺寸/mm145排料口調(diào)節(jié)范圍/mm20～50主電動機功率/KW110生產(chǎn)能力/(t/h)110～168附表3 PYD1750/100短頭型圓錐破碎機破碎機總重/t破碎機直徑/mm1750給料口尺寸/mm100給料尺寸/mm8排料口調(diào)節(jié)范圍/mm5～15主電動機功率/KW155生產(chǎn)能力/(t/h)75～230附表4 振動篩類型圓振動篩型號與規(guī)格2YAH1542工作面積/m2篩網(wǎng)層數(shù)/層2最大給料粒度/mm200處理量/th1110～385篩孔尺寸/mm30～150雙振幅/mm振次/次/min845篩面傾角/176。20電動機型號Y160L4電動機功率/KW15外形尺寸（長寬高）/mm433127152675質(zhì)量/t附表5 球磨機類型濕式格子型球磨機型號與規(guī)格MQG36003900有效容積/m336筒體轉(zhuǎn)速/rmin118最大裝球量/t80生產(chǎn)能力/t95～110傳動電動機功率/KW1250傳動電動機電壓/V6000外形尺寸（長寬高）/mm1350077006300質(zhì)量/t170附表6 水力旋流器旋流器直徑/mmΦ500給礦口/mm14020溢流口/mmΦ150沉砂口/mmΦ68～17錐角/(176。)20錐體高度/mm1090圓筒高度/mm380溢流管深度/mm300溢流粒度/mm～沉砂濃度/%50～60礦漿處理量/m3h124～108質(zhì)量/kg640附表7 攪拌槽類型浮選用型號RJ3150槽子直徑/mm3150槽子深度/mm3150槽子容積/m322葉輪直徑/mm788葉輪轉(zhuǎn)速/rmin1194；170傳動電動機功率/KW15；11質(zhì)量/t附表8 浮選機型號BSK8有效容積/m38葉輪直徑/mm650葉輪轉(zhuǎn)速/rmin1180刮板轉(zhuǎn)速/r/min16～18充吸氣量/ m3min14～10處理礦漿量/m3min11～8電動機傳動型號Y180L6電動機傳動功率/KW15電動機泡沫刮板型號Y90L6電動機泡沫刮板功率/KW外形尺寸/mm 長2250外形尺寸/mm 寬2250外形尺寸/mm 高1700附表9 濃縮機類型中心傳動型號NZS15主要用途精尾脫水內(nèi)徑/m15深度/m沉淀面積/m2 池底176提耙高度/m傳動電動機功率/KW處理量/td1390質(zhì)量/t13附表10 壓濾機型號XMZ200/1200過濾面積/m2200框內(nèi)尺寸/mm12001200濾板數(shù)量/個70總過濾面積/m2200濾瓶容量/L3541型式明流工作計示壓力/MPa～電動機功率/KW外形尺寸(長寬高)/mm851032003730質(zhì)量/t濾餅厚度/mm35卸料時間/min16附圖1 中細(xì)碎車間平面圖 附圖12 中細(xì)碎車間剖面圖 附圖23 磨礦浮選車間斷面圖 附圖34 磨礦浮選車間平面圖 附圖45 設(shè)備形象聯(lián)系圖 附圖56 工藝流程圖 附圖67 數(shù)質(zhì)量流程圖 附圖78 礦漿流程圖 附圖89 設(shè)備明細(xì)表 附圖9附錄1英文文獻(xiàn)“Method for processing goldbearing sulfide ores involving preparation of a sulfide concentrate”The present invention involves a method for processing goldbearing sulfide ores to facilitate recovery of gold from the sulfide ore. In particular, the present invention involves flotation processing of goldbearing sulfide ores in a manner that reduces problems associated with conventional flotation to produce an ore concentrate. The present invention also involves the flotation processing in bination with oxidative treating, such as pressure oxidation, and use of byproduct gas from an oxygen plant used to supply oxygen gas for the oxidative treating. Significant amounts of gold are found in sulfide ores, in which the gold is associated with sulfide mineralogy. The gold is difficult to recover from such sulfide ores, because the gold is typically bound in sulfide mineral grains in a manner that renders the ore refractory to many traditional gold recovery techniques, such as direct cyanidation of the ore. Therefore, sulfide ores are monly treated to chemically alter the sulfide mineral to permit dissolution of the gold during subsequent gold recovery operations. One technique for treating a goldbearing sulfide ore in preparation for gold recovery is to subject the ore to an oxidative treatment to oxidize sulfide sulfur in the sulfide minerals, thereby rendering the gold more susceptible to recovery. One method for oxidatively treating a sulfide ore is pressure oxidation, in which a slurry of the ore is subjected to oxygen gas in an autoclave at elevated temperature and pressure to depose the sulfide mineral, freeing the gold for subsequent recovery. Other oxidative treating methods include roasting and biooxidation of the ore in the presence of air or oxygen gas. Treating whole ores by pressure oxidation or by oxidative roasting is expensive. Part of the expense is due to energy consumed in heating goldbarren gangue material in the whole ore, and especially the energy required to heat water in which the gangue material is slurried in the case of pressure oxidation. Also, process equipment for treating a whole ore must be sized to acmodate the throughout of gangue material, in addition to the throughput of the goldbearing sulfide minerals, thereby significantly adding to the cost of process equipment. Moreover, side reactions may occur involving gangue material which can detrimentally affect the oxidative treating or can produce hazardous materials which require special handling. One way to reduce the high energy and process equipment costs associated with oxidative treating of a whole ore, as well as the potential for problems associated with side reactions, would be to remove gangue material from the ore prior to the oxidative treatment. For example, one method that has been used to remove gangue material from goldbearing sulfide ores is flotation. In flotation, air is bubbled through a slurry of ore particles which have been treated with reagents and the particles of the ore which are less hydrophilic tend to attach to and rise with the air bubbles, thereby permitting separation of the ore into two fractions. Flotation has been used to prepare concentrates of goldbearing sulfide minerals which are rich in the sulfide minerals and relatively free of gangue material. One problem with flotation of many goldbearing sulfide ores, however, is that a significant amount of the goldbearing sulfide mineral often reports to the wrong flotation fraction, representing a significant loss