{"title":"示范研究:堆浸垫排水溶液的处理:原理验证实验研究1","authors":"C. Bucknam, C. Hager","doi":"10.21000/JASMR13010136","DOIUrl":null,"url":null,"abstract":"A 20-week bench-scale study was conducted by Golder Associates to determine whether passive treatment could effectively remove weak and dissociable (WAD) cyanide and NO3 from the drain down solution emanating from a decommissioned gold heap leach pad. An anaerobic treatment scenario was chosen and three different substrates were chosen. Limestone at 10% by weight was in all three reactors, two of the reactors had between 80 and 90% hay/straw, and a third reactor had 45% hay/straw and 45 % potato mash. These are local agricultural products and by-products. Because the historic concentration of nitrate-N ranged from 142 to 297 mg/L, the flow rate into the reactors was based on the hydraulic retention time needed to remove nitrate-N down to 10 mg/L, and this was determined to be 20 days. All three substrates were effective at removing WAD cyanide and nitrate-N to below 0.04 mg/L and 1.0 mg/L, respectively. In the effluents, other constituents that could be the products of cyanide and nitrate-N degradation were analyzed and only ammonia- N was detected at concentrations from 5 to 10 mg/L. The most recent regulatory reference value has been set at 10 mg/L N for the total N in all nitrogen species. Under this monitoring requirement, the sum of nitrate-N and ammonia-N would be below the 10 mg/L N reference value.","PeriodicalId":17230,"journal":{"name":"Journal of the American Society of Mining and Reclamation","volume":"102 1","pages":"136-150"},"PeriodicalIF":0.0000,"publicationDate":"2013-03-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"DEMONSTRATION STUDY: TREATMENT OF HEAP LEACH PAD DRAIN DOWN SOLUTION: PROOF-OF-PRINCIPLE BENCH STUDY 1\",\"authors\":\"C. Bucknam, C. Hager\",\"doi\":\"10.21000/JASMR13010136\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"A 20-week bench-scale study was conducted by Golder Associates to determine whether passive treatment could effectively remove weak and dissociable (WAD) cyanide and NO3 from the drain down solution emanating from a decommissioned gold heap leach pad. An anaerobic treatment scenario was chosen and three different substrates were chosen. Limestone at 10% by weight was in all three reactors, two of the reactors had between 80 and 90% hay/straw, and a third reactor had 45% hay/straw and 45 % potato mash. These are local agricultural products and by-products. Because the historic concentration of nitrate-N ranged from 142 to 297 mg/L, the flow rate into the reactors was based on the hydraulic retention time needed to remove nitrate-N down to 10 mg/L, and this was determined to be 20 days. All three substrates were effective at removing WAD cyanide and nitrate-N to below 0.04 mg/L and 1.0 mg/L, respectively. In the effluents, other constituents that could be the products of cyanide and nitrate-N degradation were analyzed and only ammonia- N was detected at concentrations from 5 to 10 mg/L. The most recent regulatory reference value has been set at 10 mg/L N for the total N in all nitrogen species. Under this monitoring requirement, the sum of nitrate-N and ammonia-N would be below the 10 mg/L N reference value.\",\"PeriodicalId\":17230,\"journal\":{\"name\":\"Journal of the American Society of Mining and Reclamation\",\"volume\":\"102 1\",\"pages\":\"136-150\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2013-03-01\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Journal of the American Society of Mining and Reclamation\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.21000/JASMR13010136\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of the American Society of Mining and Reclamation","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.21000/JASMR13010136","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
DEMONSTRATION STUDY: TREATMENT OF HEAP LEACH PAD DRAIN DOWN SOLUTION: PROOF-OF-PRINCIPLE BENCH STUDY 1
A 20-week bench-scale study was conducted by Golder Associates to determine whether passive treatment could effectively remove weak and dissociable (WAD) cyanide and NO3 from the drain down solution emanating from a decommissioned gold heap leach pad. An anaerobic treatment scenario was chosen and three different substrates were chosen. Limestone at 10% by weight was in all three reactors, two of the reactors had between 80 and 90% hay/straw, and a third reactor had 45% hay/straw and 45 % potato mash. These are local agricultural products and by-products. Because the historic concentration of nitrate-N ranged from 142 to 297 mg/L, the flow rate into the reactors was based on the hydraulic retention time needed to remove nitrate-N down to 10 mg/L, and this was determined to be 20 days. All three substrates were effective at removing WAD cyanide and nitrate-N to below 0.04 mg/L and 1.0 mg/L, respectively. In the effluents, other constituents that could be the products of cyanide and nitrate-N degradation were analyzed and only ammonia- N was detected at concentrations from 5 to 10 mg/L. The most recent regulatory reference value has been set at 10 mg/L N for the total N in all nitrogen species. Under this monitoring requirement, the sum of nitrate-N and ammonia-N would be below the 10 mg/L N reference value.