水产养殖论文：两种碳源条件下水产养殖固体颗粒物生物絮凝效果的研究.doc

水产养殖论文：两种碳源条件下水产养殖固体颗粒物生物絮凝效果的研究

【中文摘要】Avnimelech在2006年指出相对于传统的水产养殖处理方法,生物絮凝技术（Bio-floc Technology,BFT）是一个新的选择,逐渐被认为是解决水产养殖产业发展所面临的环境制约和饲料成本的有效替代技术。生物絮凝技术有良好的水质处理效果并且对残饵和粪便中蛋白质进行多级利用,大大提高了蛋白质的利用率。实现生物絮凝的关键在于控制水体中的碳氮比以及碳源的种类,不同碳源会形成不同的细菌组成从而导致生物絮凝效果的差异。本实验分利用葡萄糖和醋酸钠为碳源并维持碳氮比大于15,以饲料为培养对象研究了在水产养殖固体颗粒物生物絮凝过程中沉降性能FV-5min、氨氮、亚硝态氮、硝态氮、絮体蛋白质等营养成分的含量的变化。主要包括下列两部分内容:1、两种碳源形成生物絮凝过程的比较采用饲料作为水产养殖固体颗粒物,在培养过程中饲料降解使水体中的溶解氨氮和有机碳比例失衡,根据水体中氨氮的含量分别添加葡萄糖和醋酸钠两种碳源维持碳氮比大于15,通过添加葡萄糖的系统,醋酸钠碳源的系统和不添加碳源的空白对照系统分析比较研究了在水产养殖固体颗粒物生物絮凝过程中不同碳源对沉降性能FV-5min、氨氮、亚硝态氮、硝态氮、絮体蛋白质等营养成分的含量变化的影响。经过33天的培养,最终葡萄糖系统絮体的蛋白含量30.4%,第8天达到最大沉降比36%,醋酸钠系统絮体蛋白含量34.6%,第10天达到最大沉降比34%,空白对照絮体蛋白含量26.3%,第10天达到最大沉降比58%。饲料在水中的降解过程中不断的释放氨氮和有机碳,水体中的氨氮和有机碳形成三个阶段动态的变化阶段,第一阶段微生物对氨氮和有机碳的利用小于饲料降解的氨氮和有机碳,造成氨氮和有机碳的不断升高。第二阶段微生物对氨氮和有机碳的利用和饲料降解的氨氮和有机碳相等,造成氨氮和有机碳在水中残留达到最大值。第三阶段微生物对氨氮和有机碳的利用大于饲料降解的氨氮和有机碳,造成氨氮和有机碳降低。从微生物代谢强弱的三个阶段来看,葡萄糖在第5天达到氨氮和有机碳的最大累积值,氨氮104.25mg/l,DOC 1558.4mg/l,醋酸钠在第6天氨氮112.5mg/l,DOC 1474.8mg/l。空白对照反应器在第7天氨氮117.89mg/l,DOC 286.72mg/l。葡萄糖碳源在第10天,醋酸钠在第12天,空白对照组在第15天氨氮降低到2mg/l以下。结果表明葡萄糖碳源反应器对无机氮处理效果要优于醋酸钠,但在形成絮体的蛋白质含量上要小于醋酸钠,葡萄糖和醋酸钠反应器的沉降性能FV-5min明显优于空白对照组。2、两种碳源生物絮凝处理效率的比较经过33天的生物絮凝培养,系统完全成熟,饲料降解完全水体中的三态氮和有机碳含量稳定不变。通过在各个系统中添加氯化铵来确定氨氮的去除效率,添加硝酸钾确定对硝态氮的去除效率,在试验中添加葡萄糖和醋酸钠根据碳源的消耗量确定有机碳的去除效率。实验表明:葡萄糖每小时对氨氮的平均去除率为2.42 mg/l·h-1 ,TOC消耗率为32 mg/l·h-1,每毫克氨氮平均利用DOC为13.2mg/l。硝态氮的平均去除率为18.06 mg/l·h-1,TOC消耗率为122.45 mg/l·h-1,去除每毫克硝氮所需TOC为6.78mg/l。醋酸钠每小时对氨氮的平均去除率为1.6 mg/l·h-1,TOC消耗率为17.4 mg/l·h-1,每毫克氨氮平均利用DOC为10.88mg/l.硝态氮的去除率为15.18 mg/l·h-1,TOC消耗率为79.68 mg/l·h-1,去除每毫克硝氮所需DOC为5.23mg/l。葡萄糖对氨氮和硝态氮的去除率要优于醋酸钠,但醋酸钠絮凝体的蛋白含量和沉降性能高于葡萄糖,醋酸钠的蛋白含量为38.8%,最小FV-5为28%。葡萄糖蛋白含量为32.3%,最小FV-5为30%。显微观察絮体形成过程中的变化,同一时期的显微照片比较发现葡萄糖为碳源形成絮体的速度要快于醋酸钠,体积要大于醋酸钠。形成的絮体主要以丝状菌居多,絮体较大相对蓬松。醋酸钠形成的絮体主要以杆菌为主,絮体较小相对致密。
【英文摘要】Avnimelech point out that Bio-floc Technology is an new treatment option of aquaculture solid waste which was considered as an method of bring down feed cost and environment pollution. Bio-floc Technology is good at the trement of water quality and the multilevel utilization of feed protein that can raise the feed protein operating factor. The key of Bio-floc Technology is to control the C/N and the carbon source species. Different carbon sources will bring up different bacterials thus it will result in bring up different effect of Biofloc-technology. The study used glucose and sodium acetate as the carbon source, used feed as the remnant feed and dejecta, kept C/N>15.The experiment measured changes of FV-5min, ammonia-N, nitrite-N and nitrate-N,pertion of flocs .This study include the following two main contents:1 The comparison of different carbon sources impact on the formation of bioflocsBecause use the feed as the Aquaculture solid particulate,through the culture of biofloc becteria the dissolved ammonia-N and organic carbon were not satiated the C/N>15, so add the different carbon sources which is glucose and sodium acetate to satiate the C/N>15. Through the comparison of FV-5min, ammonia-N, nitrite-N and nitrate-N and pertion of flocs content to analyze the different effect on Biofloc-technology which used glucose carbon sources sodium acetate carbon sources and no carbon sources . Affter 33 days, The max ammonian and DOC of glucose on the fifth day.ammonian is 104.25mg/l,DOC is 1558.4mg/l。The max ammonian and DOC of sodium acetate on sixth day.ammonian is 112.5mg/l,DOC 1474.8mg/l。The max ammonian and DOC of No carbon on the seventh day.ammonian is 117.89mg/l,DOC 286.72mg/l。The min ammonian and DOC of glucose on the tenth day.ammonian is less 2mg/l,DOC is less 200mg/l.The min ammonian and DOC of sodium acetate on the twelfth day.ammonian is less 2mg/l,DOC is less 200mg/l. The min ammonian and DOC of no carbon on the fifteenth day.ammonian is less 2mg/l,DOC is less 200mg/l. The experiment results indicated that the glucose and sodium acetate are better than no carbon in FV-5min, the removal of ammonia-N, nitrite-N and nitrate-N,but the gulcose is worse than sodium acetate in protein content.2 The comparison of different carbon sources impact on the treatment effect of bioflocsThrough the 33 days culture , the reaction is maturation, The water quality of ammonia-N and dissolved organic carbon were stable for long time when the feed deterioration entirely. Add sufficiency carbon sources with ammonium chloride and potassium nitrate to ensure concrete utilization of the nitrogen . The experiment results indicated that the average cosume of ammonian of glucose reactor is 2.42 mg/l·h-1 ,1mg/l ammonian need 13.2mg/l DOC. The average cosume of nitrate of glucose reactor is 18.06mg/l·h-1, 1mg/l nitrate need 6.78mg/l DOC. glucose floc’s protein content is 32.3%. The average cosume of ammonian of sodium actate reactor is 1.6 mg/l·h-1 ,1mg/l ammonian need 10.88mg/l DOC. The average cosume of nitrate of sodium actate reactor is 15.18mg/l·h-1, 1mg/l nitrate need 5.23mg/l DOC. glucose floc’s protein content is 38.8%.At the same time ,the microscope photo and the common camera photo of flocs which the glucose reaction have some mold fungis and the Sodium acetate have some baciluses. The glucose flocs is biger and more intensive than the Sodium acetate flocs.
【关键词】水产养殖 固体颗粒物 生物絮凝 碳源
【英文关键词】aquaculture solid particulate biofloc-technology carbon resources
【目录】两种碳源条件下水产养殖固体颗粒物生物絮凝效果的研究

摘要

4-7

ABSTRACT

7-9

引言

12-14

第一章 水产养殖生物絮凝研究进展

14-24

1 生物絮凝现状

14-15

2 絮凝机理

15-17

2.1 DLVO

15-16

2.2 EPS胞外聚合物质

16

2.3 侨联学说

16

2.4 群体感应

16-17

3 絮体中的絮凝菌

17

3.1 絮凝菌种类

17

3.2 絮凝菌的生长代谢

17

4 影响絮体形成的因素

17-19

4.1 混合强度

17-18

4.2 DO

18

4.3 有机碳源

18

4.4 有机物负荷比率C/N

18-19

4.5 温度

19

4.6 pH值

19

4.7 TSS (Total suspended solids)

19

5 生物絮凝对水产养殖价值

19-21

5.1 对残饵和粪便的转化利用

20-21

5.2 对水体中氨氮的去除

21

6 生物絮凝技术在水产养殖中的应用

21-22

7 展望

22-24

第二章 两种碳源生物絮凝形成过程的比较

24-37

1 材料和方法

25-28

1.1 生物絮凝反应器和试验设计

25-26

1.2 试验期间的碳源补充

26-27

1.3 水质指标

27

1.4 絮凝体性质评价指标

27-28

2 实验结果与分析

28-34

2.1 三态氮变化

28-29

2.1.1 氨氮

28

2.1.2 亚硝态氮和硝态氮

28-29

2.2 溶解有机碳DOC、氨氮和DOC/TAN

29-31

2.3 pH值

31-32

2.4 DO

32-33

2.5 沉降比FV-5 变化

33

2.6 营养成份

33-34

3 讨论

34-35

4 结论

35-37

第三章 两种碳源生物絮凝处理效果的比较

37-53

1：材料和方法

37-39

1.1 生物絮凝反应器和试验设计

37-38

1.2 试验期间各反应器添加的碳源、氯化铵、硝酸钾

38-39

1.3 水质指标

39

1.4 絮凝体性质评价指标

39

2. 实验结果与分析

39-50

2.1:三态氮处理效果

39-43

2.1.1 三态氮变化

39-40

2.1.2:pH 值

40-41

2.1.3: DO

41-42

2.1.4: FV-5

42

2.1.5:营养成分

42-43

2.2:氨氮处理效果

43-47

2.2.1 氨氮

43-44

2.2.2:pH 值

44-45

2.2.3: DO

45

2.2.4: FV-5

45-46

2.2.5:营养成分

46-47

2.3: 硝态氮处理效果

47-50

2.3.1 硝氮

47-48

2.3.2:pH 值

48

2.3.3: DO

48-49

2.3.4: FV-5

49-50

3 絮体表观特征

50-51

4 讨论

51-53

结论

53-54

参考文献

54-61

硕士期间发表论文

61-62

致谢

62