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氟硅酸、硼酸制备氟硼酸钾工艺研究 总被引:1,自引:0,他引:1
详细介绍了利用磷肥副产的氟硅酸和硼酸反应生产高附加值的氟硼酸钾的工艺方法。通过对工艺的研究,叙述了该工艺的反应原理、工艺流程、工艺控制、主要设备及设备的优越性。通过实验表明,利用氟硅酸中的氟与硼酸反应生产氟硼酸和白炭黑,氟硼酸与氯化钾反应生成氟硼酸钾的方法可行。氟、硼反应温度在75~85 ℃、时间为2.5~3 h转化率较高,氯化钾需按理论量加入,产品质量稳定。该工艺利用磷肥行业副产的氟硅酸制备氟硼酸钾,将氟硅酸中的氟转化为氟硼酸钾,硅转化为白炭黑,不仅实现了资源综合利用,而且将生产废弃物转化为新的产品创造了新的利润增长点,节约了化石资源萤石,同时较氢氟酸法成本有大幅度下降,该方法将会成为未来氟硼酸钾生产的发展趋势。 相似文献
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由青海大柴旦钠硼解石矿中提取硼酸,找出了最佳工艺条件,即:矿粒细度〈1.7mm,反应温度80~90℃,反应液酸度(pH)2~3,结晶温度20~25℃,反应液中硼酸质量分数15%~16%,蒸发过程镁离子质量分数〈4%,渣带失(以三氧化二硼计)质量分数〈2%。在此条件下对其工艺技术的稳定性、可靠性及适应性进行了研究。结果表明,硼的总收率达85%以上,利用本地资源生产硼酸,投资少,见效快。 相似文献
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在自行建立的管式反应器上,采用实验室开发的NY-2催化剂,以环氧乙烷(EO)吸收溶液和CO2为原料,进行合成碳酸乙烯酯(EC)连续过程研究.考察液空速、吸收溶液中EC与乙二醇(EG)摩尔比、EC与EO摩尔比、水含量、催化剂用量、反应压力和温度对反应的影响.通过实验研究,确定了较佳的连续反应条件:反应温度为(125±5)℃、反应压力为(3.5±0.5)MPa、催化剂质量分数不小于2%、吸收溶液中水的质量分数少于1.2%、EC与EO摩尔比为5、EG质量分数小于30%、空速小于0.67h^-1。在此条件下,EO的转化率大于98%,EC的选择性大于80%. 相似文献
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介绍炼厂酸性气制硫酸装置的工艺过程。由于实供气源与设计值有较大出入,二氧化碳浓度偏高, 并且夹带烃类物质较多,使装置无法正常运行。通过对酸性气进行预处理后,一次开车成功,各项工艺指标均达到设计要求,遇酸性气流量突降时可补充适量硫磺,维持正常生产。 相似文献
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在作者开发的高速反应器一步法制专用级次磷酸钠的基础上进一步将生成的次磷酸钠和副产的亚磷酸氢钙用离子膜电渗析法制成纯度更高的次磷酸及亚磷酸产品,产品质量升级,回收利用了副产亚磷酸氢钙,并减少了原料烧碱的用量。该新工艺成本低,能耗小,无三废排出,产品多样化,属循环经济、环境友好新工艺。 相似文献
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介绍了用氟硅酸制备氟硼酸的试验研究、工艺流程、设备投资情况。本工艺反应温度 70~95℃ ,反应时间 1~ 4h ,硼酸用量比 ( 0 .9~ 1 .2 )∶1 ,氟硅酸浓度要求≥ 1 6%。产品氟硼酸浓度≥ 40 %。 相似文献
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CLA production from ricinoleic acid by lactic acid bacteria 总被引:3,自引:0,他引:3
The ability to produce CLA from ricinoleic acid is widely distributed in lactic acid bacteria. Washed cells of Lactobacillus plantarum JCM 1551 were selected as a potential catalyst for CLA production from ricinoleic acid. Cells cultivated in medium supplemented
with a mixture of α-linolenic acid and linoleic acid showed enhanced CLA productivity. Under optimal reaction conditions,
with the free acid form of ricinoleic acid as the substrate and washed cells of L. plantarum as the catalyst, 2.4 mg/mL CLA was produced from 3.4 mg/mL ricinoleic acid in 90 h, with a molar yield with respect to ricinoleic
acid of 71%. The CLA produced, which was obtained in the FFA form, consisted of a mixture of two CLA isomers, cis-9,trans-11-octadecadienoic acid (21% of total CLA) and trans-9,trans-11-octadecadienoic acid (79% of total CLA), and accounted for 72% of the total FA obtained. 相似文献
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云天化云峰分公司产能为P2O5 280kt/a磷酸装置存在硫酸消耗偏高问题,分析磷酸生产中硫酸消耗偏高的原因,从合理配矿、改善矿浆粒度、控制萃取SO3含量、改善过滤状况等方面提出了降低硫酸消耗的技改措施。技改后,每吨P2O5硫酸消耗由2.628t降为2.512t。 相似文献
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Shigenobu Kishino Jun Ogawa Yoriko Omura Kenji Matsumura Sakayu Shimizu 《Journal of the American Oil Chemists' Society》2002,79(2):159-163
After screening 14 genera of lactic acid bacteria, Lactobacillus plantarum AKU 1009a was selected as a potential strain for CLA production from linoleic acid. Washed cells of L. plantarum with high levels of CLA production were obtained by cultivation in a nutrient medium with 0.06% (wt/vol) linoleic acid (cis-9,cis-12-octadecadienoic acid). Under the optimal reaction conditions with the free form of linoleic acid as the substrate, washed
cells of L. plantarum produced 40 mg CLA/mL reaction mixture (33% molar yield) from 12% (wt/vol) linoleic acid in 108 h. The resulting CLA was
a mixture of two CLA isomers, cis-9,trans-11 (or trans-9,cis-11)-octadecadienoic acid (CLA1, 38% of total CLA) and trans-9,trans-11-octadecadienoic acid (CLA2, 62% of total CLA), and accounted for 50% of the total FA obtained. A higher yield (80% molar
yield to linoleic acid) was attained with 2.6% (wt/vol) linoleic acid as the substrate in 96 h, resulting in CLA production
of 20 mg/mL reaction mixture [consisting of CLA1 (2%) and CLA2 (98%)] and accounting for 80% of total FA obtained. Most of
the CLA produced was associated with the cells (ca. 380 mg CLA/g dry cells), mainly as FFA. 相似文献
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