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S参数解释范文

S参数解释范文

S参数解释范文S参数(S-parameters)是一种广泛用于描述高频电路或微波电路的电气特性的参数,它能够提供与时域(时间域)相对应的频域(频率域)的信息。

S参数由四个值组成,分别是S11、S21、S12和S22、其中,S11表示输入端反射系数(reflection coefficient at input),即当信号从传输线的输入端进入器件时,一部分信号被反射回传输线的比例。

S21表示传输系数(transmission coefficient),它表示了从输入端到输出端的信号通过器件的转移效果。

S12表示输出端的反射系数,即当信号从输出端进入器件时,一部分信号被反射回输出端的比例。

S22表示输出端的传输系数。

S参数是通过将器件连接到网络分析仪(Network Analyzer)上测量得到的。

网络分析仪通过分别在输入端和输出端施加不同的信号,并测量相应的反射和传输信号的幅度和相位差来计算S参数。

S参数广泛应用于高频电路和微波电路的设计和分析中。

通过测量和分析S参数,可以了解器件的反射、传输和散射特性,进而优化电路的性能。

S参数还可以用于电路的建模和仿真,帮助工程师预测电路在不同工作条件下的性能。

S参数的解释需要考虑以下几个方面:1.幅度和相位:S参数包括幅度和相位两个方面的信息。

幅度表示信号的大小或衰减情况,相位表示信号的延迟或相位差。

通过分析S参数的幅度和相位信息,可以了解信号在电路中的传播和变化情况。

2.反射系数:S参数中的S11和S22表示反射系数,即信号从输入端或输出端反射回传输线的比例。

反射系数的大小决定了信号在电路中的反射程度,反射系数越小,则表示电路的匹配度越好。

3.传输系数:S参数中的S21和S12表示传输系数,即信号从输入端传输到输出端的比例。

传输系数的大小决定了信号在电路中的传输效果,传输系数越大,则表示电路具有更好的传输性能。

4.频率依赖性:S参数是频率域的参数,因此其值会随着频率的变化而变化。

asiii码表阿斯克码表大全文档

asiii码表阿斯克码表大全文档
八进制
十六进制
十进制
字符
八进制
十六进制
十进制
字符
00
00
0
nul
100
40
64
@
01
01
1
soh
101
41
65
A
02
02
2
stx
102
42
66
B
03
03
3
etx
103
43
67
C
04
04
4
eot
104
44
68
D
05
05
5
enq
105
45
69
E
06
06
6
ack
106
46
70
F
07
07
7
bel
107
47
71
dc1
121
51
81
Q
22
12
18
dc2
122
52
82
R
23
13
19
dc3
123
53
83
S
24
14
20
dc4
124
54
84
T
25
15
21
nak
125
55
85
U
26
16
22
syn
126
56
86
V
27
17
23
etb
127
57
87
W
30
18
24
can

asiii码表阿斯克码表大全文档

asiii码表阿斯克码表大全文档
(可编辑word,文选整理,文档对您有用,可收藏)
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ASCII码表
信息在计算机上是用二进制表示的,这种表示法让人理解就很困难。因此计算机上都配有输入和输出设备,这些设备的主要目的就是,以一种人类可阅读的形式将信息在这些设备上显示出来供人阅读理解。为保证人类和设备,设备和计算机之间能进行正确的信息交换,人们编制的统一的信息交换代码,这就是ASCII码表,它的全称是“美国信息交换标准代码”。
76
118
v
67
37
55
7
167
77
119
w
70
38
56
8
170
78
120
x
71
39
57
9
171
79
121
y
72
3a
58
:
172
7a
122
z
73
3b
59
;
173
7b
123
{
74
3c
60
<
174
7c
124
|
75
3d

ASCII表对照

ASCII表对照

so si dle dc1 dc2 dc3 dc4 nak syn etb can em sub esc fs gs re us sp ! " #
116 117 120 121 122 123 124 125 126 127 130 131 132 133 134 135 136 137 140 141 142 143
$ % & ` ( ) * + , . / 0 1 2 3 4 5 6 7 8 9
144 145 146 147 150 151 152 153 154 155 156 157 160 161 162 163 164 165 166 167 170 171
64 65 66 67 68 69 6a 6b 6c 6d 6e 6f 70 71 72 73 74 75 76 77 78 79
100 101 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121
d e f g h i j k l m n o p q r s t u v w x y
72 73 74 75 76 77
3a 3b 3c 3d 3e 3f
12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31
FF CR SO SI DLE DCI DC2 DC3 DC4 NAK SYN TB CAN EM SUB ESC FS GS RS US
44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63
44 45 46 47 50 51 52 53 54 55 56 57 60 61 62 63 64 65 66 67 70 71

1-s2.0-S0024379513004217-main

1-s2.0-S0024379513004217-main
Linear Algebra and its Applications 439 (2013) 2479–2493
Contents lists available at SciVerse ScienceDirect
Linear Algebra and its Applications
/locate/laa
where i = 1, . . . , n. Then we have |x| = T z x, where z = sign x ∈ Y n . For a given interval matrix A = [ A c − A , A c + A ] ∈ IRm×n , and for each vector y ∈ Y m and each vector z ∈ Y n , we introduce the matrices
m
b
b ,
where b, b ∈ R , and b b . The set of all m-by-n interval matrices will be denoted by IRm×n and the set of all m-dimensional interval vectors by IRm . Denote by A c and A the center and radius matrices given by
Ac =
1 2 1 2
( A + A ),
A
= ( A − A ),
2
1
respectively. Then A = [ A c − A , A c + A ]. Similarly, the center and radius vectors are defined as

常用ASCII码对照表

常用ASCII码对照表

常用ASCII码对照表1. ASCII码在计算机内部,所有的信息最终都表示为一个二进制的字符串。

每一个二进制位(bit)有0和1两种状态,因此八个二进制位就可以组合出256种状态,这被称为一个字节(byte)。

也就是说,一个字节一共可以用来表示256种不同的状态,每一个状态对应一个符号,就是256个符号,从0000000到。

上个世纪60年代,美国制定了一套字符编码,对英语字符与二进制位之间的关系,做了统一规定。

这被称为ASCII码,一直沿用至今。

ASCII码一共规定了128个字符的编码,比如空格“SPACE”是32(十进制的32,用二进制表示就是00100000),大写的字母A是65(二进制01000001)。

这128个符号(包括32个不能打印出来的控制符号),只占用了一个字节的后面7位,最前面的1位统一规定为0。

2、非ASCII编码英语用128个符号编码就够了,但是用来表示其他语言,128个符号是不够的。

比如,在法语中,字母上方有注音符号,它就无法用ASCII码表示。

于是,一些欧洲国家就决定,利用字节中闲置的最高位编入新的符号。

比如,法语中的é的编码为130(二进制)。

这样一来,这些欧洲国家使用的编码体系,可以表示最多256个符号。

但是,这里又出现了新的问题。

不同的国家有不同的字母,因此,哪怕它们都使用256个符号的编码方式,代表的字母却不一样。

比如,130在法语编码中代表了é,在希伯来语编码中却代表了字母Gimel (),在俄语编码中又会代表另一个符号。

但是不管怎样,所有这些编码方式中,0—127表示的符号是一样的,不一样的只是128—255的这一段。

至于亚洲国家的文字,使用的符号就更多了,汉字就多达10万左右。

一个字节只能表示256种符号,肯定是不够的,就必须使用多个字节表达一个符号。

比如,简体中文常见的编码方式是GB2312,使用两个字节表示一个汉字,所以理论上最多可以表示256x256=65536个符号。

最全ASCII码对照表[1]

最全ASCII码对照表[1]

最全ASCII码对照表Bin Dec Hex 缩写/字符解释0000 0000 0 00 NUL (null) 空字符0000 0001 1 01 SOH (start of handing) 标题开始0000 0010 2 02 STX (start of text) 正文开始0000 0011 3 03 ETX (end of text) 正文结束0000 0100 4 04 EOT (end of transmission) 传输结束0000 0101 5 05 ENQ (enquiry) 请求0000 0110 6 06 ACK (acknowledge) 收到通知0000 0111 7 07 BEL (bell) 响铃0000 1000 8 08 BS (backspace) 退格0000 1001 9 09 HT (horizontal tab) 水平制表符0000 1010 10 0A LF (NL line feed, new line) 换行键0000 1011 11 0B VT (vertical tab) 垂直制表符0000 1100 12 0C FF (NP form feed, new page) 换页键0000 1101 13 0D CR (carriage return) 回车键0000 1110 14 0E SO (shift out) 不用切换0000 1111 15 0F SI (shift in) 启用切换0001 0000 16 10 DLE (data link escape) 数据链路转义0001 0001 17 11 DC1 (device control 1) 设备控制1 0001 0010 18 12 DC2 (device control 2) 设备控制2 0001 0011 19 13 DC3 (device control 3) 设备控制3 0001 0100 20 14 DC4 (device control 4) 设备控制4 0001 0101 21 15 NAK (negative acknowledge) 拒绝接收0001 0110 22 16 SYN (synchronous idle) 同步空闲0001 0111 23 17 ETB (end of trans. block) 传输块结束0001 1000 24 18 CAN (cancel) 取消0001 1001 25 19 EM (end of medium) 介质中断0001 1010 26 1A SUB (substitute) 替补0001 1011 27 1B ESC (escape) 溢出0001 1100 28 1C FS (file separator) 文件分割符0001 1101 29 1D GS (group separator) 分组符0001 1110 30 1E RS (record separator) 记录分离符0001 1111 31 1F US (unit separator) 单元分隔符0010 0000 32 20 空格0010 0001 33 21 !0010 0010 34 22 "0010 0011 35 23 #0010 0100 36 24 $0010 0101 37 25 %0010 0110 38 26 &0010 0111 39 27 "0010 1001 41 29 ) 0010 1010 42 2A * 0010 1011 43 2B + 0010 1100 44 2C , 0010 1101 45 2D - 0010 1110 46 2E . 0010 1111 47 2F / 0011 0000 48 30 0 0011 0001 49 31 1 0011 0010 50 32 2 0011 0011 51 33 3 0011 0100 52 34 4 0011 0101 53 35 5 0011 0110 54 36 6 0011 0111 55 37 7 0011 1000 56 38 8 0011 1001 57 39 9 0011 1010 58 3A : 0011 1011 59 3B ; 0011 1100 60 3C < 0011 1101 61 3D = 0011 1110 62 3E > 0011 1111 63 3F ? 0100 0000 64 40 @0100 0001 65 41 A 0100 0010 66 42 B 0100 0011 67 43 C 0100 0100 68 44 D 0100 0101 69 45 E 0100 0110 70 46 F 0100 0111 71 47 G 0100 1000 72 48 H 0100 1001 73 49 I 0100 1010 74 4A J 0100 1011 75 4B K 0100 1100 76 4C L 0100 1101 77 4D M 0100 1110 78 4E N 0100 1111 79 4F O 0101 0000 80 50 P 0101 0001 81 51 Q 0101 0010 82 52 R0101 0100 84 54 T 0101 0101 85 55 U 0101 0110 86 56 V 0101 0111 87 57 W 0101 1000 88 58 X 0101 1001 89 59 Y 0101 1010 90 5A Z 0101 1011 91 5B [ 0101 1100 92 5C \ 0101 1101 93 5D ] 0101 1110 94 5E ^ 0101 1111 95 5F _ 0110 0000 96 60 `0110 0001 97 61 a 0110 0010 98 62 b 0110 0011 99 63 c 0110 0100 100 64 d 0110 0101 101 65 e 0110 0110 102 66 f 0110 0111 103 67 g 0110 1000 104 68 h 0110 1001 105 69 i 0110 1010 106 6A j 0110 1011 107 6B k 0110 1100 108 6C l 0110 1101 109 6D m 0110 1110 110 6E n 0110 1111 111 6F o 0111 0000 112 70 p 0111 0001 113 71 q 0111 0010 114 72 r 0111 0011 115 73 s 0111 0100 116 74 t 0111 0101 117 75 u 0111 0110 118 76 v 0111 0111 119 77 w 0111 1000 120 78 x 0111 1001 121 79 y 0111 1010 122 7A z 0111 1011 123 7B { 0111 1100 124 7C | 0111 1101 125 7D }0111 1111 127 7F DEL (delete) 删除ESC键VK_ESCAPE (27)回车键:VK_RETURN (13)TAB键:VK_TAB (9)Caps Lock键:VK_CAPITAL (20)Shift键:VK_SHIFT ()Ctrl键:VK_CONTROL (17)Alt键:VK_MENU (18)空格键:VK_SPACE (/32)退格键:VK_BACK (8)左徽标键:VK_LWIN (91)右徽标键:VK_LWIN (92)鼠标右键快捷键:VK_APPS (93)Insert键:VK_INSERT (45)Home键:VK_HOME (36)Page Up:VK_PRIOR (33)PageDown:VK_NEXT (34)End键:VK_END (35)Delete键:VK_DELETE (46)方向键(←):VK_LEFT (37)方向键(↑):VK_UP (38)方向键(→):VK_RIGHT (39)方向键(↓):VK_DOWN (40)F1键:VK_F1 (112)F2键:VK_F2 (113)F3键:VK_F3 (114)F4键:VK_F4 (115)F5键:VK_F5 (116)F6键:VK_F6 (117)F7键:VK_F7 (118)F8键:VK_F8 (119)F9键:VK_F9 (120)F10键:VK_F10 (121)F11键:VK_F11 (122)F12键:VK_F12 (123)Num Lock键:VK_NUMLOCK (144)小键盘0:VK_NUMPAD0 (96)小键盘1:VK_NUMPAD0 (97)小键盘2:VK_NUMPAD0 (98)小键盘3:VK_NUMPAD0 (99)小键盘4:VK_NUMPAD0 (100)小键盘5:VK_NUMPAD0 (101)小键盘6:VK_NUMPAD0 (102) 小键盘7:VK_NUMPAD0 (103) 小键盘8:VK_NUMPAD0 (104) 小键盘9:VK_NUMPAD0 (105) 小键盘.:VK_DECIMAL (110) 小键盘*:VK_MULTIPLY (106) 小键盘+:VK_MULTIPLY (107) 小键盘-:VK_SUBTRACT (109) 小键盘/:VK_DIVIDE (111) Pause Break键:VK_PAUSE (19) Scroll Lock键:VK_SCROLL (145)。

1-s2.0-S0360544213007809-main

1-s2.0-S0360544213007809-main

Unveiling the mystery of Combined Heat&Power(cogeneration) Aviel Verbruggen a,*,1,Pierre Dewallef b,Sylvain Quoilin b,Michael Wiggin ca University of Antwerp,Belgiumb Energy Systems Research Unit,University of Liège,Belgiumc P.Eng J Michael Wiggin Consulting Inc.,Ottawa,Canadaa r t i c l e i n f oArticle history:Received29April2013Received in revised form12September2013Accepted13September2013Available online5October2013Keywords:CHP merit and qualityDesign power-to-heat ratioVirtual bliss pointElectricity e Heat production possibility set CHP paradox a b s t r a c tThe article unveils the mystery of cogeneration.Cogeneration is an add-on or embedded activity in thermal power plants,with as merit the use of part or whole of their point source heat exhausts.EU’s talk of“high-efficiency cogeneration”is an unfounded transfer of responsibility from the hosting thermal power generation plant onto CHP(Combined Heat&Power)activity.The quality of a CHP activity is univocally defined by its design power-to-heat ratio s,a tombstone parameter derived from the design characteristics of the power plant.A thermal power plant may house more than one cogeneration ac-tivity.Identifying s requires positioning the bliss point in the electricity e heat production possibility set of the cogeneration activity.The bliss point is where after electric output is maximized,the sum of that output and the maximum recoverable quantity of heat occurs.Once CHP’s mystery of virtual bliss points is unveiled,the proper s are found.With known s by CHP activity,the quantity of cogenerated electricity is reliably assessed as best indicator of cogeneration performance.Our analysis is applicable on all relevant thermal power cycles that host CHP activities,and illustrated with a numerical example.Our lean method is necessary and sufficient for proper CHP regulation.Ó2013Elsevier Ltd.All rights reserved.1.IntroductionCogeneration or CHP(Combined Heat&Power)is as old as its natural cradle,the thermal power plant.CHP is applied in thermal power plants employing diverse technologies and ranging from a few kW to a few hundreds of MW[1].Cogeneration diffusion in countries with similar economies is uneven,due to diverging en-ergy policies and related regulations[2,3].Dedicated sector orga-nizations(COGEN Europe,Euroheat&Power,International District Energy Association)support CHP deployment.The overwhelming breakthrough has not yet arrived.CHP is not fancy.Now and then,it is embraced by policy circles[4],kindling the hope for a boost of its application.Public policy in favor of efficient fuel use,argues sup-port for cogeneration.This was intended by the EU CHP directive 2004/8/EC[5],but not realized by lack of effective and efficient regulation.The EU[6]admitted that the2004CHP directive“failed to fully tap the energy saving potential”,but shows no assessment of theflaws in its regulation.The EU continues the2004frame-work,now incorporated in the Energy Efficiency Directive[7],without any improvement in answering the essential questions that impede improved regulation of cogeneration activity and its support:What is quality of CHP?What is CHP merit?How exactly to monitor and measure CHP performance?A partial remedy was suggested by CEN(European Committee for Standardization)[8], but failed on crucial points[9].The adage of this article is”everything should be made as simple as possible,but not simpler”.We care extremely about didactic transparency in communicating insights on the paradoxes of joint electricity e heat generation processes[10].Cogeneration only ex-ists when heat from the plant is recovered and used(what supports the idea of‘priority to heat’);yet net power output always should be maximized(‘priority to power’).This double priority is also called the CHP paradox.Effective communication is based on clear terminology,now missing in CHP’s world.It starts with the proper definition of what cogeneration/CHP is,of the power-to-heat ratios,of cogenerated electricity,etc.We add a few essential concepts to develop our analysis of CHP for unveiling its mystery:Electricity e Heat(E e Q) production possibility sets,and bliss points[9,11].We also invoke vocabulary from the environmental sciences,like point source and nonpoint source pollution[12].The article is developed along the logic summarized in the ab-stract.Section2defines CHP or cogeneration as an activity added*Corresponding author.Prinsstraat13;BE2000Antwerp,Belgium.Tel.:þ32476 888239;fax:þ3232654420.E-mail address:aviel.verbruggen@ua.ac.be(A.Verbruggen).1www.avielverbruggen.be.Contents lists available at ScienceDirectEnergyjournal h omepage:w/locate/energy0360-5442/$e see front matterÓ2013Elsevier Ltd.All rights reserved./10.1016/j.energy.2013.09.029Energy61(2013)575e582on or embedded in a thermal power generation process.Fig.1il-lustrates that CHP activity may convert part or all of the point source (and so recoverable)thermal pollution of the power plant into used heat.This leads to the proper de finition of CHP being the recovery and use of all or part of the point source heat exhaust,otherwise being rejected to the ambient environment,by a thermal power generation plant.CHP is comparable to other environmental mitigation activities.CHP activity is not responsible for the power conversion ef ficiency of the hosting thermal power plant.EU ’s talk of “high-ef ficiency cogeneration ”and its “Primary Energy Saving ”approach are unfounded transfers of responsibility from the host-ing thermal power generation plant onto CHP activity.Section 3explains that the design power-to-heat ratio of a CHP activity par-allels the electricity conversion ef ficiency of the hosting power cycle.It shows that the design ratio is the necessary and suf ficient indicator of CHP quality.For identifying the proper design power-to-heat ratios,the positioning of bliss points is necessary.Here CHP analysts go astray when they overlook that most bliss points in practical CHP applications are virtual.The bliss point is where after electric output is maximized,the sum of this maximum and the maximum recoverable quantity of heat is reached (CHP paradox).Section 4states the basic merit of CHP activity being the use of part or all of a thermal power plant ’s point source heat exhaust,reducing heat rejection to the environment,and avoiding the use of other energy sources to obtain the used heat.Yet,the quantity of used heat is not adopted as the proper indicator of CHP perfor-mance because this implies incentives to downgrade a (expensive)power plant to the supply of heat that less expensive heat plants can deliver.The proper indicator is the quantity of cogenerated electricity,being the product of the design power-to-heat ratio and the recovered quantity of heat.As such this indicator overarches the CHP paradox,because the more heat is recovered and the more electricity is generated,the better scores the indicator.Section 5offers applied analysis.With the help of five graphs,the concepts and indicators proposed in the previous sections are implemented for all major power generation cycles:gas turbines,internal com-bustion engines,and extraction-condensing and backpressure steam turbines.Classing the cycles by temperature of their point source heat exhausts separates CHP activities without impact on the power output of the plant (e.g.CHP on reciprocating engines or gas turbines),from the ones with impact (e.g.CHP on steam tur-bines).Section 6is a short numerical example of the methods explained in Section 5.A few comments on the regulation of cogeneration activities are offered in Section 7,mainly recom-mending caution on the perverse impacts of the EU ’s externalbenchmark approach,because the latter leads to unfounded “high-ef ficiency ”calls.A conclusion is added in Section 8.Because the analysis breaks ground on an accurate de finition of what cogeneration really is,and because several basic concepts (electricity e heat production possibility sets,real and virtual bliss points,design power-to-heat ratios)are explained,perseverance and patience are requested from the reader to process the consecutive sections.Some proof readers of the article get the “eureka ”by the numerical example of Section 6,but it is not possible to provide the example without prior description of the concepts and methods.2.CHP is an activity added on/embedded in a thermal power generation processIn a thermal power generation plant,fuel is converted into a high temperature heat flow,partly turned into power,and partly discarded from the process as residual heat at lower temperature [13](Fig.1,left side).The power obtained from steam turbines,gas turbines,or internal combustion engines,is convertible into elec-tricity.2Heat rejection to the ambient environment is called ther-mal pollution [12].Pollution is often classed as point source or nonpoint source pollution.A point source is a single identi fiable localized source,from which flux or flow is emanating,manageable for capture,treatment,or storage.Nonpoint sources cause diffuse emissions,spreading and mixing with flows and mass in the ambient environment.In thermal power generation cycles,point sources are the con-densers at the end of the steam expansion in steam turbines,out-lets of gas turbines,and radiators for engine mantle and oil cooling.Flue gas stacks are thermal point sources when heat is still recov-erable,or are diffuse sources when non-recoverable.Heat radiation at various parts of the process is also considered non-recoverable.CHP or cogeneration is the recovery and use of all or part of the point source heat exhaust,otherwise being rejected ,by a thermal power generation plant.Fig.1represents CHP activity as a valve splitting the point source heat exhaust flow in a used andrejectedFig.1.Thermal power generation:CHP is the recovery of (a share of)the point source heat exhaust.2Few applications are direct drive (for example running a compressor on a turbine ’s shaft power),except for delivering torque or thrust for transport (vehicles,ships,planes).Fuel cells also convert (hydrogen)fuel in power and heat,but are not widely applied yet.A.Verbruggen et al./Energy 61(2013)575e 582576share:in position0no heat is used/all heat is rejected to the ambient environment;in position0.3thirty percent of the heat is used/seventy percent is rejected;in position0.6sixty percent is used/forty percent rejected;in position1all heat is used/no heat is rejected to the environment.The continuum of positions reflects all imaginable operational CHP activities.In practice CHP activity may be constrained by the design and the availability of specific facilities for recovering or for rejecting heat.For example,a steam turbine thermal power plant may be designed as a condensing power unit without possibility of using the point source heat exhaust(fixed at position0);when designed as full backpressure unit it isfixed at position1and cannot reject point source heat to the ambient environment;when facilities are installed for recovering a maximum of thirty percent of the point source heat exhaust,CHP activity can range over all positions be-tween0and0.3,but not beyond the latter.In the latter case, confusion arises,and is strengthened by dense but misleading terminology.The physical phenomenon“CHP/cogeneration activity added on or embedded in a thermal power generation plant”is mostly shortcut as“CHP/cogeneration plant”.3The shortcut obscures that CHP is an added or embedded facility to recover point source thermal pollution;as such CHP is similar to other mitigation techniques(for example scrubbers removing SO2from theflue gases of coal plants).The properties of the polluting installation may affect the mitigation facility,but the latter carries no re-sponsibility for those properties.Unfounded carrying over of re-sponsibility from the hosting thermal power generation plant onto the CHP activity is the EU’s and others talk about“high-efficiency cogeneration”[7].The merit of CHP activity is in recovering as much as possible of the point heat source exhaust.CHP activity is not responsible for the power conversion efficiency of the hosting thermal power plant.3.The quality of CHP and how to measure itThe quality of a thermal power generation process is the effi-ciency h in generating power from the fuel,measured by the ratio E/ F.In case of CHP,the cogeneration efficiency(EþQ)/F is often used as efficiency yardstick.This yardstick assigns equal weight and value to electricity and heat.However,electricity and heat do not have the same value.From the thermodynamic point of view, electricity can be entirely converted into heat or work while the conversion of heat into work is limited by the second principle of thermodynamics.From the economic point of view,expensive power plants are required to produce high-quality power while low temperature heat can be produced with not so expensive com-bustion facilities(burners,furnace,boilers,etc.).Optimizing a thermal power cycle with cogeneration activities requires maxi-mizing the output of electricity per unit of heat produced for given fuel inputs.Applying thefirst principle of thermodynamics on a thermal power plant leads to F¼EþQþL.When the diffuse losses L are stabilized at their minimum level,the efficiency ratio E/F is paral-leled by the ratio E/Q called the design power-to-heat ratio and denoted s.The latter is a crucial variable for understanding cogeneration.When h goes up,so does s,and vice versa.The quality of thermal power generation processes is reflected by the capacity to generate relatively more electricity than heat,with the ratio E/Q reflecting the quality of cogeneration.There exists a general consensus that cogeneration quality is given by the power-to-heat ratio.However,confusion is widespread on the precise definition of that ratio and on the methods to quantify the ratio. Fig.1provides the basic elements to resolve the confusion,with extended arguments and methods for assessing s values discussed in Section5.The northeast corner of Fig.1formats an electricity e heat(E,Q) diagram;the ordinate is the quantity of electricity(E)generated; the abscissa is the heat(Q)that may have been recovered from the point source heat exhaust.The words in italic in the previous sentence reveal that Q is an unsettled variable.Full recovery occurs in only a few power plants;in most power plants a(small)share of the point source heat exhaust is recovered for use.For the proper analysis of a CHP activity,the corresponding bliss point S needs identification.A bliss point in a(E,Q)diagram is the point where after E is maximized,the sum E maxþQ max(Q max being the maximum recoverable quantity of heat)is also at its maximum. In positioning the bliss point S,abstraction is made of the actual use of the point source heat exhaust.When for example,the plant is equipped to only use at maximum30%of the point source heat exhaust of the power plant,S will be a virtual bliss point.The recognition and identification of virtual bliss points,not directly observable,unveils the CHP mystery,what is crucial for the eval-uation of partial CHP activity.Once the bliss point S of a CHP activity is marked in the(E,Q) diagram of a power plant,the design power-to-heat ratio s is calculated as the slope of the vector O e S.Because s is a design attribute of the plant,s is a tombstone parameter,easy to reveal from the as built plans of the power plant with its various equip-ment and installations to manage and optimize the energyflows. When public policy meddles in the world of cogeneration,it should come up with regulations that support the maximization of s,the real quality parameter,decided during the design phase of the plant [9].This implies the maximization of electricity output,because the first goal of expensive power plants remains the provision of high-quality power,not low-quality heat.Therefore heat recovery maximization is always secondary to power maximization(see: CHP paradox and bliss point definition).4.The merit of CHP and how to measure itPublic policy may support specifically CHP activity when demonstrating particular merit(Section4.1).In case of support, what outcomes of CHP activity are adopted as proper performance indicators(Section4.2)?4.1.Specifying CHP activity meritThe visions on the merit of cogeneration in the energy economy are not universal,leading to diverging and even opposite policies ranging from stimulating to actually destroying cogeneration’s role and development[9].The basic merit of CHP activity is the use of part or all of a thermal power plant’s point source heat exhaust, reducing heat rejection to the environment,and avoiding the use of other energy sources to provide the used heat.Ceteris paribus,this merit is sufficient for ranking thermal power plants with heat re-covery facilities principally higher than its counterparts without such facilities.Adopting this merit is rooted in preferences for efficient above wasteful energy use practices that cause greenhouse gas emissions[7].The argument is weakly strengthened by refer-ence to the reduction of local climate change effects caused by concentrated waste heat releases[14].Few countries have enacted or enforce a policy with a prefer-ence for cogeneration activities.An exception is Denmark where the1979Heat Supply Act has made this priority real.The important role of cogeneration in the Danish electricity system is evident[3].3This resembles shortcut language“heat”and“work”for the proper scientificterms“energy transferred as heat”and“energy transferred as work”,emphasized bye.g.Reynolds and Perkins[13].A.Verbruggen et al./Energy61(2013)575e5825774.2.Indicators of CHP performanceAlthough the merit of CHP is in recovering all or part of therejected point source heat,the recovered quantity of heat(Q used)isnot recommendable as indicator,because for investors and opera-tors rewarding Q used holds no stimulus to maximize the designpower-to-heat ratio.Amazingly,the2009adaptations to theemissions trading scheme[15]have changed the allocation rulesfor CHP generation,such that from2013onwards CHP plants willreceive only allowances for the used heat and no longer forcogenerated power.Westner and Madlener[16]assess the negativeimpact of this rule on future investment in large-scale CHP plants.Presumably,the reason of the EU adaptation is due to persistinglack of reliable and easily auditable methods for calculating thecogenerated power output.This article offers the approach to closethis gap.Including Q used as an additional indicator with accounting forthe quality of the recovered heat is proposed by experts in ther-modynamics[17].While heat at higher temperature corresponds toa higher availability(quality)of heatflows[13],rewarding this inCHP activities counteracts the incentives to reduce the appliedtemperatures of heat end-uses in buildings and processes.Thelower the useful end-use temperatures of heating applications canbe set,the smaller is b,the used heat for generated power substi-tution rate and the higher is s,the power-to-heat ratio of CHP ac-tivities embedded in steam turbines.The necessary and sufficient CHP performance indicator is theaccurately assessed amount of cogenerated electricity E CHP.The E CHP variable is not directly observable when condensing and cogeneration activities are mixed,which is the dominant practicebecause few power plants face a sufficiently high heat demand torecover their full point source heat exhausts.E CHP is a part of themeasured E plant and has to be assessed.Generally accepted is therule E CHP¼“power-to-heat ratio”ÂQ used but lacking are defini-tion and assessment of the proper power-to-heat ratio[7e9].Section5provides the methods for assessing the proper s for every CHP activity added on or embedded in various thermal powergeneration units.With measurements of the Q usedflows,the ac-curate E CHP¼s.Q used is calculated.The remainder(E plantÀE CHP)is condensing electricity.Rewarding E CHP includes incentives tomaximize E CHP,what also means investors and operators arestimulated to maximize the design quality(s)of the CHP activity and to maximize the quantities of recovered heat(Q used).This is the appropriate way to address the joint production paradox.5.Monitoring and measuring CHP activityThe temperatures of used heat demanded have a significantimpact on some CHP activities,and on the choice of the hostingthermal power generation plants.Heat use is characterized by therequired temperature,needed for performing intended functions,such as space heating,washing,cooking,drying,eful heat isheat available at temperature sufficiently above ambient temper-ature to provide useful functions.Banding heat demand by tem-perature is recommended,for example:lowest(above ambienttemperature to50 C),low(50 e100 C),medium(100 e200 C), high(200 e400 C),very high(above400 C).Depending on the thermal power generation process,point heatsource exhausts deliver at different temperatures.Gas turbineoutlets range in the very high temperature band;at stacks of en-gines medium to high temperature heat is recoverable,and lowtemperature heat at mantle and oil coolers;the cold condensers ofsteam turbines offer massive heatflows in the lowest band.Only aminiscule part of the latter is useful for some nearby activities,suchas greenhouse or tropicalfish culture.The height of the temperature of the point source heat exhausts is a crucial discre-tionary variable for classifying cogeneration activities in two groups:CHP activities without impact on the power output of the plant,and CHP activities with impact.The former refer to“added on”,and the latter to“embedded in”CHP activity.5.1.CHP activities without impact on the power output of the plantGas turbines and internal combustion engines deliver heatflows at sufficient high temperature to match demand by a wide variety of applications.Gas turbine outlets are sufficiently hot to deliver pressurized steam for driving a steam turbine(the Combined Cycle Gas Turbine e CCGT(combined cycle gas turbine)plant).Directing their point source heat exhaust to used heat does not significantly affect the electricity output of such plants.Fig.2a and b show representative shapes of their(E,Q)production possibility sets.In these cases,the coefficient b is zero.When running the plant at full load,and an electricity output of E max is obtained,the discarded point source heat Q max¼FÀE maxÀL.The bliss point S is located at the coordinate(Q max,E max).When all that heat is used,the“bliss point”S is actually reached,maximizing the energy conversion efficiency(EþQ)/F of the plant.The design power-to-heat ratio s of this CHP activity is the slope of the vector O e S.In practical settings the demand for used heat at the plant may always be lower than the maximum recoverable heatflow Q max, and the capacity of the heat recovery facilities will be limited to the peak heat demand Q peak demand.The production possibility setisFig.2.(a)Cogeneration(E,Q)production possibility set of gas turbines and of internal combustion engines.(b)Truncated cogeneration(E,Q)production possibility set of gas turbines and of internal combustion engines.A.Verbruggen et al./Energy61(2013)575e582 578truncated.The bliss point becomes a virtual point,which results in it being overlooked.However,identi fication of the virtual bliss point is a necessity for a proper assessment of the design power-to-heat ratio s .5.2.CHP activities with impact on the power output of the plant Steam turbines are the main hosts of CHP activities.The tem-perature of their point source heat exhaust is scantly above the ambient temperature,hence not widely useful,although the flows are massive due to the latent heat of condensing the steam rejected at the end of the turbine.Practical heat uses require higher than near ambient temperatures,which necessitates steam extraction at higher temperature and pressures.For optimizing steam cycles,small steam flows are extracted from the turbines,and re-used in the cycles.Steam extracted for external heat demand before the end of a turbine where cold condensing conditions prevail,shortens the expansion path,i.e.reduces the work delivered and the power generated [13].A Mollier diagram offers a visible steam expansion path,which segment lengths re flect the amount of po-wer extracted.Fig.3a shows how cogeneration is embedded in a steam cycle that is equipped with cold condensers (approaching near vacuum pressure conditions for the steam outlet)to function as an only cold condensing plant.For clarity of the argument here it is assumed all steam flow can also be extracted either at a low or at a high backpressure (BP).To describe the production possibility sets of CHP activities,first consider the full cold condensingstatus of the turbine:E cond electricity is generated,and the point heat source exhaust equals Q cond .Because Q cond has no economic value,one increases the temperature of the exhaust,viz.the backpressure to BP-low.This reduces the electric output to E BP-low ,and enlarges the point source heat flow to Q BP-low ;this substitution of used heat for generated power is generally called “power loss ”(we prefer the term “used heat for generated power substitution ”),with b as common symbol.The value of b is evidently dependent on the backpressure experienced by the turbine ’s steam flow [18].Fig.3a shows two levels of backpressure (low and high),with production possibility sets respectively triangle O e E cond e S BP-low ,and O e E cond e S BP-high (both truncated by minimum plant load constraints).Their used heat for generated power substitution rates differ,with as a corollary that their design power-to-heat ratios differ.Generalizing the argument reveals that a continuum of backpressures or hot condensing temperatures are feasible,each one de fining another CHP activity embedded in the steam turbine power plant.Every CHP activity is characterized by its speci fic b and s ,crossing in the speci fic bliss point S BP .Fig.3a also shows the continuum of bliss points,as a segment of the line re flecting the first principle of thermodynamics F ÀL ¼E þQ,with the diffuse losses L stabilized at their minimum level [9].The ratio of latent to sensible heat in the total heat flow decreases with higher back-pressure,as visually shown by more declining E cond e S BP lines (caused by higher b values).The incremental heat for power sub-stitution,by higher backpressure relative to a lower backpressure,is re flected in the (equal to À1)slope of the set of bliss points.In practice,a steam turbine may have two major hot condensers for steam extraction.Assuming all steam can be extracted at all three condensers (one cold þtwo hot),the production possibility set of the steam plant is shown by area O e E cond e S BP-low e S BP-high e O .Generally,the heat extraction capacity at large steam plants will be limited by the demanded heat capacity of the end-uses (e.g.,the base load of a district heating system).This is shown in Fig.3b,derived from Fig.3a.The actual possibility set of the plant is the solid bordered pentagon,as a cut from the wider set dis-cussed in Fig.3a.When only viewing the smaller set without the virtual components underlying the set,it is dif ficult to recognize the crucial parameters,such as the proper design power-to-heat ratio.Assessing E CHP is done first by CHP activity:the heat recovery Q used at every hot condenser is measured and multiplied bytheFig.3.(a)Cogeneration (E ,Q )production possibility set of extraction-condensing steam turbines.(b)Truncated cogeneration (E ,Q )production possibility set of extraction-condensing steamturbines.Fig. 4.Cogeneration (E ,Q )production possibility set of pure backpressure steam turbines.A.Verbruggen et al./Energy 61(2013)575e 582579。

asiii码表阿斯克码表大全之欧阳地创编

asiii码表阿斯克码表大全之欧阳地创编
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121
51
81
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22
12
18
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122
52
82
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23
13
19
dc3
123
53
83
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24
14
20
dc4
124
54
84
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25
15
21
nak
125
55
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26
16
22
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126
56
86
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27
17
23
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127
57
87
W
30
18
24
can
130
58
88
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31
19
25
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131
59
89
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32
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时间:2021.03.04
创作:欧阳地
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67
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167
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70
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72
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73
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59
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ASCII码值对照表

ASCII码值对照表

最全ASC‎I I码对照‎表 ASCII‎码值对照表‎ASCII‎码值 ASCII‎码中英文对‎照表0010 0000 32 20 空格0010 0001 33 21 !0010 0010 34 22 "0010 0011 35 23 #0010 0100 36 24 $0010 0101 37 25 %0010 0110 38 26 &0010 0111 39 27 '0010 1000 40 28 (0010 1001 41 29 )0010 1010 42 2A *0010 1011 43 2B +0010 1100 44 2C ,0010 1101 45 2D -0010 1110 46 2E .0010 1111 47 2F /0011 0000 48 30 00011 0001 49 31 10011 0010 50 32 20011 0011 51 33 30011 0100 52 34 40011 0101 53 35 50011 0110 54 36 60011 0111 55 37 70011 1000 56 38 80011 1001 57 39 90011 1010 58 3A :0011 1011 59 3B ;0011 1100 60 3C <0011 1101 61 3D =0011 1110 62 3E >0011 1111 63 3F ?0100 0000 64 40 @0100 0001 65 41 A0100 0010 66 42 B0100 0011 67 43 C0100 0100 68 44 D0100 0101 69 45 E0100 0110 70 46 F0100 0111 71 47 G0100 1000 72 48 H0100 1001 73 49 I0100 1010 74 4A J0100 1011 75 4B K0100 1100 76 4C L0100 1101 77 4D M0100 1110 78 4E N0100 1111 79 4F O0101 0000 80 50 P0101 0001 81 51 Q0101 0010 82 52 R0101 0011 83 53 S0101 0100 84 54 T0101 0101 85 55 U0101 0110 86 56 V0101 0111 87 57 W0101 1000 88 58 X0101 1001 89 59 Y0101 1010 90 5A Z 0101 1011 91 5B [ 0101 1100 92 5C \ 0101 1101 93 5D ] 0101 1110 94 5E ^ 0101 1111 95 5F _ 0110 0000 96 60 ` 0110 0001 97 61 a 0110 0010 98 62 b 0110 0011 99 63 c 0110 0100 100 64 d 0110 0101 101 65 e 0110 0110 102 66 f 0110 0111 103 67 g 0110 1000 104 68 h 0110 1001 105 69 i 0110 1010 106 6A j 0110 1011 107 6B k 0110 1100 108 6C l 0110 1101 109 6D m 0110 1110 110 6E n 0110 1111 111 6F o 0111 0000 112 70 p 0111 0001 113 71 q 0111 0010 114 72 r 0111 0011 115 73 s 0111 0100 116 74 t 0111 0101 117 75 u 0111 0110 118 76 v 0111 0111 119 77 w 0111 1000 120 78 x 0111 1001 121 79 y 0111 1010 122 7A z 0111 1011 123 7B { 0111 1100 124 7C | 0111 1101 125 7D } 0111 1110 126 7E ~ 0111 1111 127 7F DEL (delet‎e) 删除ESC键 VK_ES‎C APE (27)回车键: VK_RE‎T URN (13) TAB键: VK_TA‎B (9)Caps Lock键‎: VK_CA‎P ITAL‎(20) Shift‎键: VK_SH‎I FT ()Ctrl键‎: VK_CO‎N TROL‎(17) Alt键: VK_ME‎N U (18)空格键: VK_SP‎A CE (/32)退格键: VK_BA‎C K (8)左徽标键: VK_LW‎I N (91)右徽标键: VK_LW‎I N (92)鼠标右键快‎捷键:VK_AP‎P S (93) Inser‎t键: VK_IN‎S ERT (45) Home键‎: VK_HO‎M E (36) Page Up: VK_PR‎I OR (33) PageD‎o wn: VK_NE‎X T (34)End键: VK_EN‎D (35)Delet‎e键: VK_DE‎L ETE (46)方向键(←): VK_LE‎F T (37)方向键(↑): VK_UP‎(38)方向键(→): VK_RI‎G HT (39)方向键(↓): VK_DO‎W N (40)F1键: VK_F1‎(112)F2键: VK_F2‎(113)F3键: VK_F3‎(114)F4键: VK_F4‎(115)F5键: VK_F5‎(116)F6键: VK_F6‎(117)F7键: VK_F7‎(118)F8键: VK_F8‎(119)F9键: VK_F9‎(120)F10键: VK_F1‎0 (121)F11键: VK_F1‎1 (122)F12键: VK_F1‎2 (123)Num Lock键‎: VK_NU‎M LOCK‎(144)小键盘0: VK_NU‎M PAD0‎(96)小键盘1: VK_NU‎M PAD0‎(97)小键盘2: VK_NU‎M PAD0‎(98)小键盘3: VK_NU‎M PAD0‎(99)小键盘4: VK_NU‎M PAD0‎(100)小键盘5: VK_NU‎M PAD0‎(101)小键盘6: VK_NU‎M PAD0‎(102)小键盘7: VK_NU‎M PAD0‎(103)小键盘8: VK_NU‎M PAD0‎(104)小键盘9: VK_NU‎M PAD0‎(105)小键盘.: VK_DE‎C IMAL‎(110)小键盘*: VK_MU‎L TIPL‎Y (106)小键盘+: VK_MU‎L TIPL‎Y (107)小键盘-: VK_SU‎B TRAC‎T (109)小键盘/: VK_DI‎V IDE (111)Pause‎Break‎键: VK_PA‎U SE (19)Scrol‎l Lock键‎: VK_SC‎R OLL (145)注意:1.在ASCI‎I码中,有4组字符‎:一组是控制‎字符,如LF,CR等,其对应AS‎C II码值‎最小;第2组是数‎字0~9,第3组是大‎写字母A~Z,第4组是小‎写字母a~z。

ASCII码对照表

ASCII码对照表

好用的ASCII 码对照表完整版信息在计算机上是用二进制表示的,这种表示法让人理解就很困难。

因此计算机上都配有输入和输出设备,这些设备的主要目的就是,以一种人类可阅读的形式将信息在这些设备上显示出来供人阅读理解。

为保证人类和设备,设备和计算机之间能进行正确的信息交换,人们编制的统一的信息交换代码,这就是ASCII 码表,它的全称是“美国信息交换标准代码ASCII 码对照表在Web开发时,如下的ASCII 码只要加上&#和; 就可以变成Web可以辨认的字符了在处理特殊字符的时候特别有用,如:' 单引号在数据库查询的时候是杀手,但是如果转换成'(注意:转换后的机构有:&# +字符的ASCII码值+; 三个部分组成)再来存数据库,就没有什么影响了。

其他的字符与ASCII 码的对照如下表键盘常用ASCII 码ESC键VK_ESCAPE (27) 回车键:VK_RETURN (13) TAB键:VK_TAB (9) Caps Lock 键:VK_CAPITAL (20) Shift 键:VK_SHIFT ($10) Ctrl 键:VK_CONTROL (17) Alt 键:VK_MENU (18) 空格键:VK_SPACE ($20/32) 退格键:VK_BACK (8) 左徽标键:VK_LWIN (91) 右徽标键:VK_LWIN (92) 鼠标右键快捷键:VK_APPS (93)Insert 键:VK_INSERT (45) Home键:VK_HOME (36)Page Up:VK_PRIOR (33) PageDown:VK_NEXT (34) End键:VK_END (35)Delete 键:VK_DELETE (46) 方向键(←):VK_LEFT (37) 方向键(↑):VK_UP(38) 方向键(→):VK_RIGHT (39) 方向键(↓):VK_DOWN (40)F1键:VK_F1 (112)F2键:VK_F2 (113)F3键:VK_F3 (114)F4键:VK_F4 (115)F5键:VK_F5 (116)F6键:VK_F6 (117)F7键:VK_F7 (118)F8键:VK_F8 (119)F9键:VK_F9 (120)F10键:VK_F10 (121)F11键:VK_F11 (122)F12键:VK_F12 (123)Num Lock 键:VK_NUMLOCK (144) 小键盘0:VK_NUMPAD0 (96)小键盘1:VK_NUMPAD0 (97) 小键盘2:VK_NUMPAD0 (98) 小键盘3:VK_NUMPAD0(99) 小键盘4:VK_NUMPAD0 (100) 小键盘5:VK_NUMPAD0 (101) 小键盘6:VK_NUMPAD0 (102) 小键盘7:VK_NUMPAD0 (103) 小键盘8:VK_NUMPAD0 (104) 小键盘9:VK_NUMPAD0 (105) 小键盘.:VK_DECIMAL (110) 小键盘*:VK_MULTIPLY (106) 小键盘+:VK_MULTIPLY (107) 小键盘-:VK_SUBTRACT (109) 小键盘/:VK_DIVIDE (111)Pause Break 键:VK_PAUSE (19)Scroll Lock 键:VK_SCROLL (145)enjoy the trust of 得到...的信任have / put trust in 信任in trust 受托的,代为保管的take ...on trust 对...不加考察信以为真trust on 信赖give a new turn to 对~~ 予以新的看法turn around / round 转身,转过来,改变意见turn back 折回,往回走turn ⋯away 赶走⋯⋯,辞退⋯⋯,把⋯⋯打发走,转脸不睬,使转变方向turn to ⋯转向⋯⋯,( for help )向⋯⋯求助,查阅,变成;着手于think through ⋯思考⋯⋯直到得出结论,想通think of 想到,想起,认为,对⋯⋯有看法/ 想法。

最全ASCII码对照表

最全ASCII码对照表

最全ASCII 码对照表Bin Dec Hex 缩写/字符解释0000 0000 0 00 NUL (null) 空字符0000 0001 1 01 SOH (start of handing) 标题开始0000 0010 2 02 STX (start of text) 正文开始0000 0011 3 03 ETX (end of text) 正文结束0000 0100 4 04 EOT (end of transmission) 传输结束0000 0101 5 05 ENQ (enquiry) 请求0000 0110 6 06 ACK (acknowledge) 收到通知0000 0111 7 07 BEL (bell) 响铃0000 1000 8 08 BS (backspace) 退格0000 1001 9 09 HT (horizontal tab) 水平制表符0000 1010 10 0A LF (NL line feed, new line) 换行键0000 1011 11 0B VT (vertical tab) 垂直制表符0000 1100 12 0C FF (NP form feed, new page) 换页键0000 1101 13 0D CR (carriage return) 回车键0000 1110 14 0E SO (shift out) 不用切换0000 1111 15 0F SI (shift in) 启用切换0001 0000 16 10 DLE (data link escape) 数据链路转义0001 0001 17 11 DC1 (device control 1) 设备控制1 0001 0010 18 12 DC2 (device control 2) 设备控制2 0001 0011 19 13 DC3 (device control 3) 设备控制3 0001 0100 20 14 DC4 (device control 4) 设备控制4 0001 0101 21 15 NAK (negative acknowledge) 拒绝接收0001 0110 22 16 SYN (synchronous idle) 同步空闲0001 0111 23 17 ETB (end of trans. block) 传输块结束0001 1000 24 18 CAN (cancel) 取消0001 1001 25 19 EM (end of medium) 介质中断0001 1010 26 1A SUB (substitute) 替补0001 1011 27 1B ESC (escape) 溢出0001 1100 28 1C FS (file separator) 文件分割符0001 1101 29 1D GS (group separator) 分组符0001 1110 30 1E RS (record separator) 记录分离符1F US (unit separator) 单元分隔符0001 1111 310010 0000 32 20 空格0010 0001 33 21 !0010 0010 34 22 I!0010 0011 35 23 #0010 0100 36 24 $0010 0101 37 25 %0010 0110 38 26 &0010 0111 39 27 I!0010 1001 41 29 ) 0010 1010 42 2A * 0010 1011 43 2B + 0010 1100 44 2C J 0010 1101 45 2D - 0010 1110 46 2E0010 1111 47 2F / 0011 0000 48 30 0 0011 0001 49 31 1 0011 0010 50 32 2 0011 0011 51 33 3 0011 0100 52 34 4 0011 0101 53 35 5 0011 0110 54 36 6 0011 0111 55 37 7 0011 1000 56 38 8 0011 1001 57 39 9 0011 1010 58 3A0011 1011 59 3B J 0011 1100 60 3C < 0011 1101 61 3D = 0011 1110 62 3E > 0011 1111 63 3F ? 0100 0000 64 40 @0100 0001 65 41 A 0100 0010 66 42 B 0100 0011 67 43 C 0100 0100 68 44 D 0100 0101 69 45 E 0100 0110 70 46 F 0100 0111 71 47 G 0100 1000 72 48 H 0100 1001 73 49 I 0100 1010 74 4A J 0100 1011 75 4B K 0100 1100 76 4C L 0100 1101 77 4D M 0100 1110 78 4E N 0100 1111 79 4F O 0101 0000 80 50 P0101 0001 81 51 Q 0101 0010 82 52 R0101 0100 84 54 T0101 0101 85 55 U 0101 0110 86 56 V 0101 0111 87 57 W 0101 1000 88 58 X 0101 1001 89 59 Y 0101 1010 90 5A Z 0101 1011 91 5B [ 0101 1100 92 5C \ 0101 1101 93 5D ] 0101 1110 94 5E A0101 1111 95 5F0110 0000 96 60 '0110 0001 97 61 a 0110 0010 98 62 b 0110 0011 99 63 c 0110 0100 100 64 d 0110 0101 101 65 e 0110 0110 102 66 f 0110 0111 103 67 g 0110 1000 104 68 h 0110 1001 105 69 i 0110 1010 106 6A j 0110 1011 107 6B k 0110 1100 108 6C l 0110 1101 109 6D m 0110 1110 110 6E n 0110 1111 111 6F o 0111 0000 112 70 p 0111 0001 113 71 q 0111 0010 114 72 r 0111 0011 115 73 s 0111 0100 116 74 t 0111 0101 117 75 u 0111 0110 118 76 v 0111 0111 119 77 w 0111 1000 120 78 x 0111 1001 121 79 y 0111 1010 122 7A z 0111 1011 123 7B { 0111 1100 124 7C | 0111 1101 125 7D }0111 1111 127 7F DEL (delete) ESC 键VK_ESCAPE (27) 回车键:VK_RETURN (13)TAB 键: VK_TAB (9) Caps Lock键:VK_CAPITAL (20) Shift 键: VK_SHIFT () Ctrl 键: VK_CONTROL (17) Alt 键:VK_MENU (18) 空格键: VK_SPACE (/32) 退格键:VK_BACK (8)左徽标键: VK_LWIN (91) 右徽标键:VK_LWIN (92)鼠标右键快捷键 : VK_APPS (93)Insert 键: VK_INSERT (45) Home 键: VK_HOME (36) Page Up :VK_PRIOR (33)PageDown : VK_NEXT (34) End 键: VK_END (35) Delete 键:VK_DELETE (46) 方向键(J ):VK_LEFT (37)方向键(T ): VK_UP (38) 方向键(T ): VK_RIGHT (39) 方向键(J ):VK_DOWN (40) F1 键: VK_F1 (112) F2 键: VK_F2 (113) F3 键: VK_F3 (114) F4 键: VK_F4 (115) F5 键: VK_F5 (116) F6 键: VK_F6 (117) F7 键: VK_F7 (118) F8 键: VK_F8 (119) F9 键: VK_F9 (120) F10 键: VK_F10 (121) F11 键: VK_F11 (122) F12 键: VK_F12 (123) Num Lock 键:VK_NUMLOCK (144) 小键盘 0 :VK_NUMPAD0 (96) 小键盘 1 : VK_NUMPAD0 (97) 小键盘 2 : VK_NUMPAD0 (98) 小键盘 3 : VK_NUMPAD0 (99) 小键盘 4 : VK_NUMPAD0 (100)小键盘 5 : VK_NUMPAD0 (101)0111 1110 126 7E删除小键盘6 :VK_NUMPAD0 (102) 小键盘7 :VK_NUMPAD0 (103) 小键盘8 :VK_NUMPAD0 (104) 小键盘9 :VK_NUMPAD0 (105) 小键盘. :VK_DECIMAL (110) 小键盘* :VK_MULTIPLY (106) 小键盘+ :VK_MULTIPLY (107) 小键盘- :VK_SUBTRACT (109) 小键盘/ :VK_DIVIDE (111) Pause Break 键:VK_PAUSE (19) Scroll Lock 键:VK_SCROLL (145)。

sybase错误码

sybase错误码

sybase错误码Sybase 错误代码是一组错误代码集,用于所有 Sybase 产品,包括 Adaptive Server Enterprise。

Adaptive Server Anywhere 所返回的每个Sybase 错误代码,都有与之匹配的Adaptive Server Anywhere 错误代码。

在许多情况下,Adaptive Server Anywhere 错误代码比对应的Sybase 错误代码更详细,因此,下表中的某些Sybase 错误代码并不是唯一的。

Sybase 错误代码 Adaptive Server Anywhere SQLCODE 错误消息0 –631 RAISERROR 被执行:%1102 –171 打开游标时出错102 –199 在游标上的 INSERT/_delete 只能修改一个表102 –933 IQ 数据库需要日志102 –275 在运行时服务器中不支持触发器和过程102 –273 在触发器动作中不允许执行 COMMIT/ROLLBACK102 –131 '%1' 附近有语法错误 %2102 –687 语法错误,未指定 IQ PATH 时不能指定 IQ 特定选项102 –875 无法连接到 '%1'102 –145 未找到外键名 '%1'102 –271 触发器定义与现有触发器冲突102 –272 触发器定义中的 REFERENCES 子句无效102 –635 不允许在视图上对列权限 GRANT102 –151 子查询只允许一个选择列表项102 –269 不能删除或重命名触发器定义中引用的列103 –250 标识符 '%1' 过长104 –854 ORDER BY 子句中对 '%1' 的函数或列引用无效108 –152 ORDER BY 说明无效133 –262 未找到标签 '%1'134 –261 已有名为 '%1' 的变量137 –260 未找到变量 '%1'154 –623 过程或触发器中不允许数据定义语句155 –200 无效的选项 '%1' —不存在 PUBLIC 设置174 –154 函数 '%1' 的参数数目错误176 –611 不支持的 Transact-SQL 功能176 –148 未知函数 '%1'182 –159 无效的列号201 –639 调用过程 '%1' 时参数名遗失201 –615 在过程 '%2' 中未找到参数 '%1'201 –737 签名 '%1' 与过程参数不匹配205 –153 UNION、INTERSECT 或 EXCEPT 中的 _select 列表长度不匹配207 –124 从表 '%1' 中删除的列多于定义的列207 –143 未找到列 '%1'208 –142 未找到相关名 '%1'209 –144 在多个表中找到列 '%1' —需要相关名209 –163 派生表 '%1' 没有列 %2 的名称213 –207 _insert 的值数目错误217 –274 过程或触发器调用嵌套太深220 –158 值 %1 超出了目标的范围230 –191 无法修改表 '%2' 中的列 '%1'230 –190 不能更新表达式233 –195 表 '%2' 中的列 '%1' 不能为 NULL233 –733 已超出所允许的 NULL 的列数限制257 –157 无法将 %1 转换为 %2257 –705 从过程 '%1' 返回的 void 类型不能在任何表达式中使用262 –121 权限被拒绝:%1264 –637 重复的插入列285 –708 READTEXT 或 WRITETEXT 语句无法引用视图301 –147 出现多种将 '%1' 连接到 '%2' 的方法301 –680 Transact-SQL 外连接的 WHERE 子句中的表达式无效301 –146 无法将 '%1' 连接到 '%2'305 –681 Transact-SQL 外连接中使用的连接类型无效311 –295 无法唯一标识游标中的行314 –122 操作将引起组循环315 –136 表 '%1' 在外连接循环中315 –137 表 '%1' 需要唯一的相关名401 –134 未实现功能 '%1'401 –135 语言扩充401 –156 '%1' 附近的表达式无效401 –994 函数或过程 '%1' 的参数过多404 –890 语句大小或复杂程度超过服务器限制409 109 集合函数中的空值已删除409 –90 过程 '%2' 的参数 '%1' 不能为空504 –265 未找到过程 '%1'509 –140 用户 ID '%1' 不存在512 –186 子查询不能返回多个行518 103 无效的数据转换532 104 上次读取后行已更新532 106 表 '%2' 中列 '%1' 的值已更改538 –627 在 '%1' 附近的语法中检测到不允许的语言扩充546 –194 表 '%2' 中的外键 '%1' 没有主键值547 –198 表 '%1' 中行的主键被表 '%3' 中的外键 '%2' 引用547 –677 表 '%1' 有带参照动作的外键548 –196 表 '%2' 的索引 '%1' 将不唯一548 –209 违反了约束 '%1':表 '%3' 中列 '%2' 的值无效549 –729 无法强制使用指定的外键 (%1)550 –632 在基表'%1' 中插入/更新时违反了WITH CHECKOPTION553 –264 FETCH 中的变量数错误554 –208 上次读取后行已更改—操作被取消557 –853 游标未处于有效状态557 –170 尚未声明游标558 –172 游标已打开559 –180 游标未打开560 100 未找到行560 –197 没有当前的游标行573 –738 口令至少必须有 %1 个字符590 111 语句无法执行601 –642 无效的 SQL 描述符名708 –80 无法启动数据库服务器708 –86 没有足够的内存来启动708 –679 分配给 Java 虚拟机用于远程访问的内存不足709 –996 找不到指定的本地连接。

asiii码表阿斯克码表大全文档

asiii码表阿斯克码表大全文档
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Highly active magnetic bismuth tungstate/magnetite composite under visible light irradiation in the presence of hydrogenperoxideGuoqiang Shan,Yu Fu,Xiaolong Chu,Chun Chang,Lingyan Zhu ⇑Key Laboratory of Pollution Processes and Environmental Criteria,Ministry of Education,Tianjin Key Laboratory of Environmental Remediation and Pollution Control,Collegeof Environmental Science a r t i c l e i n f o Article history:Received 18October 2014Accepted 20December 2014Available online 31December 2014Keywords:Bi 2WO 6Fe 3O 4Visible light Magnetic Rhodamine BHydroxyl radicalsa b s t r a c tBi 2WO 6/Fe 3O 4composites were synthesized using hydrothermal method and their photocatalytic activity to degrade rhodamine B (RhB)under visible light irradiation assisted with H 2O 2and underlying mecha-nisms were investigated.The composites were 3D flower-like microspheres constructed by 2D Bi 2WO 6nanosheets loaded with spherical Fe 3O 4nanoparticles.The composited photocatalysts could be easily harvested from the reaction solution by an external magnetic field.In the presence of H 2O 2,a large amount of hydroxyl radicals (ÅOHs)were produced by H 2O 2reacting with photogenerated electrons.Fe 3O 4not only promoted the separation of hole–electron pairs but also acted as a Fenton-like reagent,expediting the production of ÅOH.Thus,the composites in the presence of H 2O 2displayed much higher photocatalytic efficiency to degrade RhB than pure Bi 2WO 6.98%of RhB (initial concentration 10mg/L)was degraded in 2h visible irradiation and 60%of total organic carbon (TOC)was removed in 3h by 0.5g/L Bi 2WO 6/Fe 3O 4(5:1).The composite displayed high photodegradation efficiency at pH 3–9.Our study suggests that a visible light driven and highly active magnetic photocatalyst-Fenton coupling oxi-dation system may have potential application in water treatment and environmental cleaning.Ó2015Elsevier Inc.All rights reserved.1.IntroductionIn recent years,semiconductor photocatalytic process has found its wide application in water treatment as a low-cost,environmen-tal friendly and sustainable treatment technology [1].TiO 2is one of the most widely applied photocatalysts under irradiation of ultraviolet light.However,TiO 2can only absorb ultraviolet wave-length,which constitutes only $3–5%of solar light [2].In order to make better use of sunlight in nature,efforts have been done to develop catalysts which are active to visible light.Bismuth phot-ocatalysts,including Bi 2WO 6,are active to visible light and display potential photocatalytic efficiency to many contaminants and azo dyes under visible light irradiation [3–7].As a visible-light-driven photocatalyst,Bi 2WO 6displays potential catalytic capacity to many organic chemicals under irradiation of visible light and it is primarily synthesized by hydrothermal or solvothermal method [8].In order to improve catalytic efficiency,Bi 2WO 6catalysts with/10.1016/j.jcis.2014.12.0680021-9797/Ó2015Elsevier Inc.All rights reserved.⇑Corresponding author at:The College of Environmental Science and Engineer-ing,NankaiUniversity,Weijin Road 94,Tianjin 300071,PR China.Fax:+862223508807.E-mail address:zhuly@ (L.Zhu).different morphology and crystal structures were synthesized [8,9].Another effective technique is to dope Bi2WO6with metal, or metal oxide,which might trap the photogenerated electrons and restrain the recombination of hole–electron pair[10–13].However,one of the shortcomings which limit the real applica-tion of these catalysts in water treatment is that it is very difficult to separate the catalysts from the reaction solution at the end of reaction without the assistance of centrifugation orfiltration. Recently,many studies have been conducted to prepare photocat-alysts with magnetic materials,which could be separated and recy-cled conveniently by applying an external magneticfield.Many magnetic iron materials,such as CoFe2O4[14],NiFe2O4[15], Fe3O4[16],were coupled with different photocatalysts to prepare composites with magnetic property.In many cases,doping with magnetic materials would reduce photocatalytic activities of the original catalysts due to decreasing activity sites available for reac-tion.Strategies are needed to prepare magnetic composites which retain the good photoactivity of the original catalyst and obtain good magnetic property.Magnetite(Fe3O4)is an ideal magnetic material and widely used in catalysis because of its low cost and easy preparation [17].Besides its ultrahigh-density magnetic property,Fe3O4has been used as heterogeneous Fenton-like catalyst for catalytic oxi-dation of organic compounds[18,19].H2O2is a typical oxidative agent and has been widely used in practical water treatment [20].As an electron capture agent,H2O2can react with photogen-erated electrons to produce hydroxyl radicals(ÅOHs)[4,21].H2O2þeÀCB!ÅOHþOHÀð1ÞThus,when H2O2is co-present with Bi2WO6/Fe3O4composite,it might interact with the composite and affect the photocatalytic capacity.It was reported that Bi2WO6and its composites such as Co3O4/Bi2WO6,C/Fe–Bi2WO6,Bi2WO6@carbon/Fe3O4exhibited higher photodegradation efficiency with the assistance of H2O2 [21–24].Xu et al.and Liu et al.synthesized Bi2WO6/Fe3O4compos-ites and achieved high degradation efficiency for RhB[25,26].How-ever,the mechanisms involved in the complex system were not fully investigated.The current study aimed to dope Bi2WO6with Fe3O4to prepare magnetic Bi2WO6/Fe3O4composites and investigate the combined degradation mechanisms of Bi2WO6/Fe3O4in the presence of H2O2. Rhodamine B(RhB)was used to imitate nonbiodegradable,toxic organic compounds with multiple benzene rings.The photocata-lytic activity of the magnetic composites to RhB under visible light (k>400nm)in the presence of H2O2was evaluated.The respective roles of Bi2WO6,Fe3O4and H2O2and the reaction mechanism were investigated extensively.The impacts of H2O2concentration and solution pH on the photocatalytic performance were studied.The degradation pathway was also investigated.The proposed strategy was useful for designing a visible light driven and magnetic photo-catalyst-Fenton coupling oxidation system for wastewater treatment.2.Materials and experiment2.1.Materials and reagentsRhodamine B(RhB)(98%)was purchased from J&K Scientific Ltd.(Beijing,China).FeCl3Á6H2O(analytical reagent,AR)was bought from Guangfu Technology Co.Ltd.(Tianjiin,China).Sodiumacetate(AR),NaOH(AR)and HNO3(65%)were purchased from Jiangtian Chemical Technology Co.Ltd.(Tianjin,China).Bi(NO3)3-Á5H2O,Na2WO4Á4H2O(AR)and KI(Guaranteed reagent)was pur-chased from Yingda Chemical Technology Co.Ltd.(Tianjin, China).Isopropanol(AR)was provided by Fengchuan Chemical Technology Co.Ltd.(Tianjin,China).AgNO3(AR)was obtained from Tairuier Chemical Co.Ltd.(Shanghai,China).Glycol and absolute ethyl alcohol(AR)were purchased from Concord Technology Co. Ltd.(Tianjin,China).Terephthalic acid(TPA)(99%)was purchased from ACROS(New Jersey,USA).124G.Shan et al./Journal of Colloid and Interface Science444(2015)123–1312.2.Preparation of nanosphere Fe3O4by solvothermal method1.35g of FeCl3was dissolved in75mL glycol,and then3.6g sodium acetate was added in the solution.After sodium acetate was dissolved completely,the solution was ultrasonicated for 30min.The mixture was transferred to a50mL autoclave,heated at200°C for16h.Then the black solid powder was separated from the solution by centrifugation,washed with deionized water and absolute ethanol consecutively and dried under120°C for5h[27].2.3.Preparation of Bi2WO6/Fe3O4and Bi2WO6A certain amount of Fe3O4was dispersed in20mL of glycol by magnetic stirring for10min and then ultrasonicated for30min. Ten mL of Bi(NO3)3solution at0.2mol/L(dissolved in1mol/L HNO3aqueous solution)was added to the dispersed Fe3O4-glycol solution.After magnetic stirring for20min,10mL of Na2WO4solu-tion at0.1mol/L(dissolved in1mol/L NaOH aqueous solution)was added dropwisely into the mixed solution.It was then stirred vig-orously for10min and ultrasonicated for30min.Xu et al.pre-pared Bi2WO6and Bi2WO6/Fe3O4(pH=1,3,5,7)and found that those prepared at pH1did not show desirable photodegradation capacity for RhB[26].Thus,to investigate the enhancement effect of H2O2,the pH of the precursor suspension was adjusted to1 using HCl.The suspension was then transferred to a50mL of Tef-80°.FT-IR spectrum was obtained by MAGNA-560Nicolet.The morphology of the photocatalyst was characterized by a Hitachi-S3500N scanning electron microscope(SEM).Brunauer–Emmett–Teller(BET)surface area measurements were performed on a Quantachrome AUTOSORB sorption analyzer.The nitrogen adsorp-tion and desorption isotherms were measured at393K after degassing the samples.Diffuse reflection spectra(DRS)were mea-sured with a Hitachi U-3010spectrometer at the range of300–700nm.Their magnetic properties(M–H curve)were measured at room temperature on a VSM9600magnetometer.Fluorescence spectra for solid and liquid samples were measured by Hitachi F-4500fluorescence spectrophotometer.2.5.Photocatalytic experimentsPhotocatalytic activity of the catalysts was evaluated by photo-catalytic degradation of RhB(10mg/L).A350W Xe lamp with 400nm lightfilter was used as light source.The loading amount of the catalysts was0.5g/L.Before adding the catalysts,the solu-tion of RhB was adjusted to pH7.0using HCl or NaOH.Before illu-mination,a certain amount of H2O2(wt.30%)was added in the suspension of the catalyst and RhB.The mixed solution was mag-netically stirred in dark for1h to ensure the establishment of an adsorption–desorption equilibrium between the catalyst and RhB.The dispersion was then exposed to visible light irradiationimages of the prepared catalysts.(A)pure Bi2WO6;(B)Fe3O4;(C)the front of Bi2WO6/Fe3O4(5:1);(D)the side of BiG.Shan et al./Journal of Colloid and Interface Science444(2015)123–13112540mL of mixed solution of NaOH(1mol/L)and absolute ethanol (v:v=1:1)was added in the vial to extract RhB remaining on the solids.The mixture was stirred for4h.The RhB concentration in the supernatant was measured by Cary UV–Vis spectrophotometer at553nm wavelength.The removal efficiency was calculated as follows:Removal rate¼ðC dþC aÞ=C iÂ100%ð2ÞC d,C a and C i are the concentrations of RhB degraded,RhB residue adsorbed on the catalysts and the initial RhB in solution, respectively.2.7.Determination ofÅOH in the reaction systemThe amount ofÅOH in the reaction system was determined by fluorescence spectrophotometer analysis method with tere-phthalic acid(TPA)capture[28,29].Four mL of TPA solution (0.2mol/L,dissolved in0.5mol/L NaOH solution)as trapping agent was added in the reaction solution.The producedÅOHs during irra-diation may react with TPA following Eq.(3)to form2-hydroxy terephthalic acid(HTPA),which was detected byfluorescence spectrophotometer(excitation wavelength at315nm,emission wavelength at about425nm).ð3Þ3.Results and discussion3.1.Materials characterizationFig.1A shows the XRD spectra of Fe3O4and Bi2WO6/Fe3O4com-posites.For Fe3O4,the diffraction peaks correspond to the standard Fe3O4(JCPDS No.65-3107),which is cubic with cell parameters as a=b=c=8.391Å,a=b=c=90°.Diffraction peaks at about31.2°, 35.5°,43.2°,57.0°and62.6°correspond to the(220)(311)(400) (511)(440)crystal planes of Fe3O4respectively[30].In the com-posites with Bi2WO6,the diffraction peaks at26.5°,28.2°,47.2°and 55.8°are attributed to the(131)(200)(202)(133)planes of Bi2-WO6(JCPDS No.39-0256)respectively[31].As the content of Fe3O4 increases,the peak intensities at35.5°,43.8°,62.5°increase consis-tently,indicating that Fe3O4was doped in Bi2WO6successfully.The FT-IR spectra of Fe3O4,Bi2WO6and Bi2WO6/Fe3O4are shown in Fig.1B.For Fe3O4,the peak at584cmÀ1corresponds to the stretching vibration of Fe–O–Fe in Fe3O4[32].In the spectrum of Bi2WO6/Fe3O4composite,the peaks at730and628cmÀ1attri-bute to Bi–O,W–O stretching and W–O–W bridge stretching modes;the peak at572cmÀ1belongs to Fe–O–Fe.As compared with pure Fe3O4,the peaks shift slightly,implying that doping with Bi2WO6may affect the Fe–O–Fe bond.Other peaks at3427and 1620cmÀ1are ascribed to the stretching and bending vibrations of free or bonded hydroxyl groups,which may be due to the mois-ture introduced in the process of mixing with KBr.The UV–vis DRS spectra are shown in Fig.1C.Pure Bi2WO6was pale yellow powder and displayed absorbing capacity in visible light region with an absorption edge at about450nm[25,33].After composited with Fe3O4,the light absorption of the Bi2WO6/Fe3O4 composites increased and extended in a wider range of200–700nm.This could be due to the dark red color of the composites after doping with Fe3O4[25].The SEM images of Bi2WO6,Fe3O4and5:1Bi2WO6/Fe3O4are shown in Fig.2.The nano-sheets of Bi2WO6with the crystallite size of about4–10nm in thickness and200–300nm in length are assembled to form particles withflower-like shape in a2l m diam-eter.The Fe3O4nanosphere particles(diameter at around200nm) were formed under the solvothermal conditions using ethylene glycol as solvent.The Fe3O4nano-particles were aggregated together due to their magnetic property.The3D morphologies of Bi2WO6/Fe3O4(5:1)composite in front and by the side indicate that nano-flakes of Bi2WO6were clustered asflower microspheres with diameter about2l m.It is clear that Fe3O4nanoparticles evenly distributed on the surface or inserted among the nanoflakes of Bi2WO6[26].The Brunauer–Emmett–Teller(BET)specific surface areas and porous volumes of Bi2WO6,Fe3O4and Bi2WO6/Fe3O4composites were determined using nitrogen adsorption and desorption iso-therms.The N2adsorption/desorption isotherms and porous struc-tures are shown in Fig.3A.The S BET of pure Bi2WO6was about 38.43cm2/g and that of Fe3O4was about27.94cm2/g.Doping Fe3O4in Bi2WO6significantly enhanced the S BET of the composites, which was53.80,58.30,47.89and55.02cm2/g for10:1,5:1,3:1 and2:1composites,respectively.The pore size of pure Bi2WO620004000distribution(inlet)of purecurves of(a)Fe3O4,(b)Bi2WOseparation of Bi2WO6/Fe3O4(5:1)of an external magnet.126G.Shan et al./Journal of Colloid and Interface Science444(2015)123–131and Bi 2WO 6/Fe 3O 4(5:1,2:1)was around 2nm and their single point total volume was 0.1018,0.1288,0.1162cm 3/g,respectively.Thus,the Bi 2WO 6/Fe 3O 4(5:1)composite had a slightly higher total volume.The magnetic behavior of pure Fe 3O 4and Bi 2WO 6/Fe 3O 4(2:1,5:1)was investigated and the results are shown in Fig.3B.The M –H hysteresis loop indicates that Fe 3O 4and Bi 2WO 6/Fe 3O 4composites possessed permanent magnetic properties.The satura-tion magnetization value (Ms )of them was 70.50,21.79,8.614emu/g respectively,which decreased significantly with decrease in the amount of Fe 3O 4in the composites.This was desir-able since the magnetic property is contributed by Fe 3O 4.Bi 2WO 6/Fe 3O 4(5:1)particles could be easily separated from the colloidal suspension by applying an external magnetic field in 5min,as shown in the lower right panel of Fig.3B.3.2.Photocatalytic performanceThe photocatalytic efficiency of the catalysts and Fe 3O 4in the absence of H 2O 2to degrade RhB is shown in Fig.4A.H 2O 2alone (10mM)displayed negligible degradation efficiency (only 4%)for RhB under visible light.Pure Fe 3O 4neither showed degradation efficiency to RhB.Pure Bi 2WO 6and Bi 2WO 6/Fe 3O 4composites,dis-played relatively high removal efficiency of 66–83%.However,most RhB removed from the solution was not degraded but strongly adsorbed on surface of catalysts.The adsorbed dye mole-attraction between RhB molecules and the catalyst surface (this will be discussed in details later).However,once the same amount of H 2O 2(10mM)was added to the reaction system,the maximum absorbance peak disappeared after 90min and no other peaks were observed in the range of 250–800nm (Fig.4B),suggesting the aromatic and azo groups of RhB were destroyed and decomposed into small molecules.This indicates that H 2O 2promoted the photocatalytic efficiency of both Bi 2WO 6and Bi 2WO 6/Fe 3O 4(Fig.4C).More than 95%RhB (10mg/L)was degraded under visible light irradiation within 2h irradiation.Less than 1–5%of RhB remained on surface of the composites (0.5g/L)at the end of irradiation.Xu et al.reported that only 67%of RhB (4.79mg/L)was removed by Bi 2WO 6/Fe 3O 4(1g/L)after 2h irradiation [26].Liu et al.reported that the removal rate of RhB (4.79mg/L)in 2h irradiation was 80%by Bi 2WO 6/Fe 3O 4com-posite (1g/L)[25].In the present study,around 39.1%,60.0%of total organic carbon (TOC)was removed by pure Bi 2WO 6and Bi 2-WO 6/Fe 3O 4(5:1)composite after 3h irradiation in the presence of H 2O 2(Fig.4D).Fu et al.reported that the complete degradation of RhB (4.79mg/L)required 20h and only 5%of TOC was removed after 3h irradiation by pure Bi 2WO 6(0.5g/L)[3].It is obvious that addition of H 2O 2greatly enhanced the photocatalytic capacity for RhB.Among the catalysts,the 5:1Bi 2WO 6/Fe 3O 4composite dis-played the highest catalytic efficiency.Thus,the 5:1composite was selected for further research.G.Shan et al./Journal of Colloid and Interface Science 444(2015)123–131127However,its underlying mechanisms remain unclear.It is well known that H2O2can accept photogenerated electron to produce ÅOH,which is a strong oxidative species to degrade organic chem-icals[21].To ascertain the impacts of H2O2on the photocatalytic capacity of Bi2WO6and Bi2WO6/Fe3O4,the amount ofÅOH in the reaction solutions was determined.Fig.5shows thefluorescence intensities of HTPA in the reaction solutions with H2O2alone, Fe3O4/H2O2,Bi2WO6/H2O2and Bi2WO6/Fe3O4/H2O2during irradia-tion.For H2O2alone,the very weakfluorescence signal suggest that negligibleÅOHs were produced under visible light irradiation (Fig.5A).This might explain the very low degradation efficiency of H2O2under simulated solar light irradiation.In the system with Fe3O4/H2O2(Fig.5B),the strong signal indicates that a large amount ofÅOHs were produced,through Fenton-like reaction as shown in Eq.(4).Surface Fe3O4(…Fe II)could decompose H2O2to produceÅOHs[18]:B Fe IIþH2O2!B Fe IIIþÅOHþOHÀð4ÞHowever,only10%of RhB was degraded in the system of Fe3O4/ H2O2(Fig.4C).This might be owing to the low adsorption capacity of Fe3O4for RhB molecules.In the system of Fe3O4/H2O2,the solu-tion pH was7.5,at which the surface of Fe3O4(p H pzc=6.8)and RhB molecules(p K a=3.0)were negatively charged.Thus,there is a strong repulsive interaction between them,leading to very weak adsorption of RhB on the surface of Fe3O4.It is well recognized that photocatalytic degradation happens on or very near to the surface of the catalysts[35].As a result,RhB could not be degraded effi-ciently in the Fe3O4/H2O2system.As illustrated in Fig.5C and D,thefluorescence signal intensities in the Bi2WO6/H2O2and Bi2WO6/Fe3O4/H2O2systems increased rapidly during irradiation of120min.In the presence of H2O2, the photogenerated electrons of Bi2WO6might react with H2O2 quickly to generateÅOHs as Eq.(1).The photodegradation of RhB by Bi2WO6/H2O2was much higher than pure Bi2WO6,implying thatÅOHs played an important role in the photodegradation under visible light irradiation.The amount ofÅOH produced in the Bi2WO6/Fe3O4/H2O2system was twice of that in the Bi2WO6/H2O2system during120min irra-diation.This might be attributed to the heterogeneous Fenton-like reaction of surface Fe3O4with H2O2just as Eq.(4)and the coupling effect occurring at the interfaces of Fe3O4and Bi2WO6,which led to effective separation of electron–holes pairs of Bi2WO6.To ascertain this latter assumption,the photoluminescence(PL)spectroscopy of Bi2WO6/Fe3O4and Bi2WO6at room temperature was measured and the results are illustrated in Fig.S1.Upon photoexicitation at 325nm,pure Bi2WO6exhibited PL band at475–525nm.However, the Bi2WO6/Fe3O4(5:1)composite exhibited much weaker PL sig-nal.The lower PL intensity of the composite suggests that doping with Fe3O4led to more separation of photo-induced hole–electron pairs[36].As a result,the production ofÅOHs by the Bi2WO6/Fe3O4 composites was enhanced compared to equal amount of pure Bi2-WO6in the presence of H2O2.This also explained the relatively higher photocatalytic degradation efficiency of the magnetic composite.To further understand the reaction mechanism of the catalysts in the presence of H2O2,isopropanol(IPA)(v:v=1:20)asÅOH scav-enger,KI(5mmol/L)as a hole scavenger and AgNO3(5mmol/L)as a photo-electron scavenger was added in the reaction systems, respectively.As shown in Fig.6A,the degradation of RhB was inhibited by the three reagents under visible light irradiation,sug-gesting thatÅOH,photoelectron and hole are related to the photo-degradation in the complex system with H2O2.It was reported that photogenerated hole oxidation might take part in the photodegra-dation process with Bi2WO6[3,37,38].However,Fig.4A shows RhB was hardly decomposed by Bi2WO6or Bi2WO6/Fe3O4without the assistance of H2O2.It is expected that the impact of hole oxidation128G.Shan et al./Journal of Colloid and Interface Science444(2015)123–131may not be notable due to the strong adsorption of RhB on the sur-face of the catalysts.As shown in Fig.6B,theÅOH generated in the system of Bi2WO6without H2O2under visible irradiation could be negligible while a large amount ofÅOHs were generated as H2O2 was added(Fig.6B).Thus,theÅOH generation owing to the addition of H2O2might be the principal pathway,particularly in the initial step of the formation of the observed N-deethylated intermediates of RhB(Scheme S1)[39].Once the adsorbed RhB was degraded by ÅOHs,the hole oxidation might then take part in the degradation of RhB.It was found that Bi2WO6/Fe3O4/H2O2displayed higher photo-catalytic efficiency to degrade RhB than Bi2WO6/H2O2.It also dis-played higher TOC removal(60%)than Bi2WO6/H2O2(39%).These suggest that Bi2WO6/Fe3O4(5:1)composite in the presence of H2O2displays stronger oxidative capacity.It may be explained by the moreÅOHs generated in the Bi2WO6/Fe3O4/H2O2system com-pared to that in the Bi2WO6/H2O2system during120min ually,the photocatalytic efficiency of the photocatalyts doped with magnetic materials decreases as compared to the ori-ginal catalysts with the same mass.For example,the degradation efficiencies of TiO2/CoFe2O4[40]and TiO2/ZnFe2O6[41]decreased significantly compared to pure TiO2due to reduced active sites available for photoactivity.However,in the present study,the pho-tocatalytic activity of the Bi2WO6/Fe3O4composites was not reduced but enhanced as compared with equal amount of pure Bi2-WO6.This suggests that doping with Fe3O4not only introduces magnetic property to the composites but also assists to enhance the photocatalytic activity.3.4.Effects of H2O2dosage and initial pHFig.7A shows the effect of H2O2with a dosage of0.1–40mM on photocatalysis of RhB by Bi2WO6/Fe3O4(5:1)composite.The deg-radation efficiency increased with increasing in the concentration of H2O2(0.1–20mM).As more H2O2was added in the solution, moreÅOHs were produced,and higher photocatalytic efficiency was resulted.However,when the concentration of H2O2was higher than20mM,the degradation efficiency decreased.This might be due to that the excess H2O2reacted withÅOHs in the solu-tion as following Eqs.(5)and(6)[42].Thus,the amount ofÅOH decreased,leading to lower photocatalytic efficiency.ÅOHþH2O2þOHÀ!H2OþHOÅ2ð5ÞÅOHþHOÅ2!H2OþO2ð6ÞSolution pH might be one of the most important factors affect-ing the adsorption and photocatalytic degradation of RhB [38,43,44].The impact of solution pH on the adsorption of Bi2WO6/ Fe3O4(5:1)is shown in Fig.7B.The adsorption capacity of the cat-alyst decreased as the initial pH increased in the range3–11.The p H pzc of Bi2WO6and Bi2WO6/Fe3O4(5:1)was determined to be 4.3(Fig.7C).RhB(p K a=3[45])molecules are negatively charged in the studied pH range.The surface of the catalyst is positively charged when the pH is lower than4.3while is negatively charged as the pH is higher than4.3.At pH3,there is a strong electrostatic attraction between RhB molecules and the catalyst surface,leading to higher adsorption affinity.With the increase of the solution pH, the interaction becomes gradually from attraction to repulsive interaction.As a result,the adsorption decreased gradually.More than50%of RhB was adsorbed on the catalyst surface at pH3–9. While only20%of RhB was adsorbed at pH11.During2h irradia-tion,RhB was degraded completely under pH3–9,as shown in Fig.7D.However,only13%of RhB was degraded at pH11.Accord-ing to Eq.(1),alkaline condition does not favor the generation of ÅOHs,which may explain the low degradation efficiency of the composite at pH11[43].The solution pH was determined before and after adding the catalysts in the system.Due to the low p H pzc (4.3)of Bi2WO6/Fe3O4(5:1),the solution pH decreased to7and10 after adding the catalyst in the reaction solution with initial pH9 and11respectively.The amount ofÅOH produced in the reaction solutions at initial pH9and11was determined.As shown in Fig.S2,the amount ofÅOH in the solution at pH9increased signif-icantly during the irradiation,whileÅOH was not detected in the solution at initial pH11,supporting that basic conditions do not favor the formation ofÅOH and the degradation efficiency decreases significantly.This suitability in a wide pH range(3–9)is vital in the practical wastewater treatment.In traditional Fenton process,the pH of wastewater inflow requires an acidic condition(about pH 3)for an ideal efficiency[46,47].The highly effective Bi2WO6/ Fe3O4/H2O2system can overcome this shortcoming and be suitable for neutral or weak alkaline conditions of wastewater.3.5.Photodegradation pathwayTo further identify the major intermediates,the reaction solu-tion was analyzed by LC/MS and GC/MS(the analytical methods are shown in SI).Intermediates at m/z443,415,387,359and 331were observed in LC/MS spectrum and they were identified as RhB,N,N,N0,-triethylated Rh,N,N0,-diethylated Rh or N,N,-diethy-lated Rh,N-ethylated Rh and Rh respectively[48,49].The reactionG.Shan et al./Journal of Colloid and Interface Science444(2015)123–131129kinetics of these species is shown in Fig.S3.As the concentration of RhB in the solution decreased with the irradiation time,the species of N,N,N0,-triethylated Rh,N,N0,-diethylated Rh or N,N,-diethylated Rh,N-ethylated Rh and Rh were produced gradually due to the consecutive N-de-ethylation.In the GC–MS results,some small organic molecules were identified in the reaction solution at irradi-ation of60and120min,and they are listed in Tables S1and S2.At irradiation of60min,some aromatic organic molecules were iden-tified,while smaller molecules without benzene ring were identi-fied in the solution after irradiation for120min.The results suggest that RhB and the N-de-ethylated intermediates were degraded mainly by ring opening in thefirst60min irradiation. Then,the produced aromatic intermediates were further degraded to small organic acids,amines and alcohols.The proposed photo-degradation pathway is shown in Scheme S1.4.ConclusionsDoping Bi2WO6with Fe3O4not only introduced strongly mag-netic property to the composites,but also enhanced the photocat-alytic capability to degrade RhB in the presence of H2O2.The generation ofÅOH due to the addition of H2O2is vital for RhB deg-radation.Fe3O4not only promoted the separation of hole–electron pairs but also acted as a Fenton-like reagent,expediting the pro-duction ofÅOHs.As a result,the composites displayed highly effi-cient photodegradation and mineralization capacities to RhB in the presence of H2O2under simulated solar light irradiation.At the end of reaction,the photocatalysts could be harvested from reaction solution easily by applying an external magneticfield.The Bi2WO6/Fe3O4in the presence of a moderate H2O2can be suit-able for wide pH conditions of wastewater.AcknowledgmentsThe authors gratefully acknowledge thefinancial support of Ministry of Science and Technology(2014CB932001, 2012ZX07529-003),Tianjin Municipal Science and Technology Commission(13JCZDJC35900),and the Ministry of Education inno-vation team(IRT13024).Appendix A.Supplementary materialFor the photoluminescence spectra of the catalysts;thefluores-cence spectra of HTPA in Bi2WO6/Fe3O4/H2O2(pH9and11);the identification of the degradation intermediates of RhB by GC/MS; the proposed photodegradation pathway of RhB,see SI.Supple-mentary data associated with this article can be found,in the online version,at /10.1016/j.jcis.2014.12.068. 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