語系:
繁體中文
English
說明(常見問題)
回圖書館首頁
手機版館藏查詢
登入
回首頁
切換:
標籤
|
MARC模式
|
ISBD
Thermophilic Anaerobic Co-digestion ...
~
Liu, Zhimin.
FindBook
Google Book
Amazon
博客來
Thermophilic Anaerobic Co-digestion of Swine Manure with Corn Stover for Biogas Production.
紀錄類型:
書目-電子資源 : Monograph/item
正題名/作者:
Thermophilic Anaerobic Co-digestion of Swine Manure with Corn Stover for Biogas Production./
作者:
Liu, Zhimin.
出版者:
Ann Arbor : ProQuest Dissertations & Theses, : 2017,
面頁冊數:
150 p.
附註:
Source: Dissertation Abstracts International, Volume: 78-10(E), Section: B.
Contained By:
Dissertation Abstracts International78-10B(E).
標題:
Agricultural engineering. -
電子資源:
http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=10610756
ISBN:
9781369856392
Thermophilic Anaerobic Co-digestion of Swine Manure with Corn Stover for Biogas Production.
Liu, Zhimin.
Thermophilic Anaerobic Co-digestion of Swine Manure with Corn Stover for Biogas Production.
- Ann Arbor : ProQuest Dissertations & Theses, 2017 - 150 p.
Source: Dissertation Abstracts International, Volume: 78-10(E), Section: B.
Thesis (Ph.D.)--North Carolina State University, 2017.
The transition of anaerobic digestion from mesophilic to thermophilic conditions using a one-step temperature jump from 35 °C to 50 °C was first studied in two continuously stirred tank reactors (CSTR) treating swine wastewater and corn stover. Both reactors were operated at constant organic loading rate of 1.074 kg VS/m3/d and hydraulic retention time (HRT) of 25 days. Although the one-step temperature jump from 35 °C to 50 °C resulted in severe fluctuation of daily methane production and volatile fatty acids concentrations, the systems reached stability after 25 days. It can be concluded that the strategy for changing temperature from mesophilic to thermophilic condition using one-step temperature jump is feasible in anaerobic CSTR treating swine wastewater and corn stover. In comparison with mesophilic anaerobic digestion, thermophilic anaerobic digestion performed better in regards to daily gas production, specific gas yield and chemical oxygen demand (COD) removal. The effects of HRT was investigated and it was shown that the system could be operated at an HRT as low as 5 days.
ISBN: 9781369856392Subjects--Topical Terms:
3168406
Agricultural engineering.
Thermophilic Anaerobic Co-digestion of Swine Manure with Corn Stover for Biogas Production.
LDR
:04837nmm a2200325 4500
001
2162683
005
20181009045509.5
008
190424s2017 ||||||||||||||||| ||eng d
020
$a
9781369856392
035
$a
(MiAaPQ)AAI10610756
035
$a
AAI10610756
040
$a
MiAaPQ
$c
MiAaPQ
100
1
$a
Liu, Zhimin.
$3
3350681
245
1 0
$a
Thermophilic Anaerobic Co-digestion of Swine Manure with Corn Stover for Biogas Production.
260
1
$a
Ann Arbor :
$b
ProQuest Dissertations & Theses,
$c
2017
300
$a
150 p.
500
$a
Source: Dissertation Abstracts International, Volume: 78-10(E), Section: B.
500
$a
Adviser: Jay J. Cheng.
502
$a
Thesis (Ph.D.)--North Carolina State University, 2017.
520
$a
The transition of anaerobic digestion from mesophilic to thermophilic conditions using a one-step temperature jump from 35 °C to 50 °C was first studied in two continuously stirred tank reactors (CSTR) treating swine wastewater and corn stover. Both reactors were operated at constant organic loading rate of 1.074 kg VS/m3/d and hydraulic retention time (HRT) of 25 days. Although the one-step temperature jump from 35 °C to 50 °C resulted in severe fluctuation of daily methane production and volatile fatty acids concentrations, the systems reached stability after 25 days. It can be concluded that the strategy for changing temperature from mesophilic to thermophilic condition using one-step temperature jump is feasible in anaerobic CSTR treating swine wastewater and corn stover. In comparison with mesophilic anaerobic digestion, thermophilic anaerobic digestion performed better in regards to daily gas production, specific gas yield and chemical oxygen demand (COD) removal. The effects of HRT was investigated and it was shown that the system could be operated at an HRT as low as 5 days.
520
$a
The effect of sodium hydroxide (NaOH), lime (Ca(OH)2) and the combined NaOH and Ca(OH)2 pretreatment on corn stover were investigated in this study. Digestions were performed in 12 L laboratory-scale CSTR operated with an organic loading rate of 1.074 kg VS/m3/d. HRT was 5 days and the operating temperature was 50 °C. The results of methane fermentation study on alkaline pretreated corn stover had resulted into significant amount of increase in biogas as well as methane yields. NaOH pretreated corn stover produced 30.95% higher biogas yield and 36.84% higher methane yield compared to the untreated corn stover. Lime pretreated corn stover had resulted into an increase of 32.43% in biogas yield and 37.50% in methane yield compared to that of untreated corn stover. Combination of NaOH and lime-treated corn stover had resulted into an increase of 38.10% in biogas yield and 44.44% in methane yield compared to that of untreated corn stover.
520
$a
The effect of total solids (TS) concentration on anaerobic co-digestion of swine manure and corn stover was further investigated in CSTR at solid content of 2.5%, 4% and 5.5%. Digestions were performed in 12 L laboratory-scale CSTR with operating temperature at 50 °C and HRT of 5 days. The daily loading of swine manure and corn stover was mixed at a mass ratio of 3:1 to achieve a carbon/nitrogen (C/N) ratio of 30 in the mixture and was diluted to desired TS concentration. The Analysis of Variance (ANOVA) showed that the gas yield from the various TS% was significantly different (p < 0.05). The results indicated that the gas yield decreased with the increase in the solid content. Higher gas yield achieved at lower TS concentration was attributed to overloading of the substrates. COD and VS reduction were the highest when the reactor was operated at TS of 2.5%.
520
$a
A mathematical model has been developed to describe the swine manure and corn stover co-digestion process. This model includes multiple-reaction stoichiometry, microbial growth kinetics with acetic acid inhibitory effects and conventional material balances for an ideally mixed reactor. The ordinary differential equations (ODE) of the model were coded in RStudioRTM software and integrated using the package deSolve. A laboratory batch experiment using swine manure and corn stover as substrates was conducted to calibrate the model. The kinetic parameters used in the model were adjusted for thermophilic conditions and were estimated using least square variation method. Bootstrap is used to estimate the standard error and 95% confidence interval of model kinetic parameters. The applicability of the model was demonstrated by comparing experimental results from literature with the model simulation results.
590
$a
School code: 0155.
650
4
$a
Agricultural engineering.
$3
3168406
650
4
$a
Environmental engineering.
$3
548583
690
$a
0775
690
$a
0539
710
2
$a
North Carolina State University.
$b
Biological and Agricultural Engineering.
$3
2103702
773
0
$t
Dissertation Abstracts International
$g
78-10B(E).
790
$a
0155
791
$a
Ph.D.
792
$a
2017
793
$a
English
856
4 0
$u
http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=10610756
筆 0 讀者評論
館藏地:
全部
電子資源
出版年:
卷號:
館藏
1 筆 • 頁數 1 •
1
條碼號
典藏地名稱
館藏流通類別
資料類型
索書號
使用類型
借閱狀態
預約狀態
備註欄
附件
W9362230
電子資源
11.線上閱覽_V
電子書
EB
一般使用(Normal)
在架
0
1 筆 • 頁數 1 •
1
多媒體
評論
新增評論
分享你的心得
Export
取書館
處理中
...
變更密碼
登入