values for fob purchase cost

8/9/2019 Values for FOB Purchase Cost

1/38

Equipment sizes and equipment costs

Size Seider

D (ft) L (ft) W (lb) W (t)

Reactor Transesterifcation 3.674541 4.41273 1131.07 0.513 2.65

Columns MeOH distillation 1.32 23 3240 1.4696 2.65

FAME drin! 1.71 ".53 207.35 0.0941 1

Mixer Feed 7.611549 9.12073 1"10 0."21 1

#as$in! Mi%er 1.15 3.6 2020.442 0.9165 1

&e'trali(ation )S*1000

Separator #as$in! Settler 3.2" 6.6 9000.76" 4.0"27 1

F+, Settlin! Tan- 4.2653 ".5306 154.3235"

Heat Exchanger+E HE%

Double ipe 623.69 57.9425

Shell ! "ube 1612.26 149.7"4

umps

(Hp#$Sg p#%&&&gal)'gitator Transesterifcation 3 0."72

Feed 10 25.73

#as$in! 5

M

' (ft*) ' (m*)

/FMor SSS ta-en as aera!e o SS 2.1 and arenter3.2


2/38

arett8s19"9 E inde% Sit$ Matches+com

357"7.334 4.16 14""75.31 155902.224124 1309.901 1753.679312 164"00

"3"75.9597 4.16 34"923.992 365393.204733 233".""2 3131.266792 40700

"104.95773 4.16 33716.6241 3530".04"7955 325."924 436.300906 7700

2365".5563 2.5 59146.390" 6193".1004176 1926.076 257".607454 61600

10201."664 2.5 25504.6661 2670".4"63657 2107."66 2"21.9"5906 25400

"2"96.4"04 4.16 344"49.359 361126.24"24 7176.063 9607.227241 :

0.002" 2"00

1." 250331.530006 2633.971 3526.32"29 137600

412396.44""47 5024.45" 6726.6"3"94 207500

1334.12135 2 266".2427 3606."6"17937 :

19003.4907 2 3"006.9"14 51376.9499649 :

3975.37075 2 7950.74149 10747.626696" :

1"00000 100000

;


3/38

214649.95025>ac-eted ? A!itated

365393.20473ol'n@ no internals@edi'

10029.154229ol'n@ no internals@edi'

"0233.233"31>ac-eted ? A!itated

330"3.1"40"Mi%erSettler

:

2"00

179222.2""56o'


4/38

+eactor.$t

essel.$t
http://www.matche.com/EquipCost/Reactor.htmhttp://www.matche.com/EquipCost/Vessel.htmhttp://www.matche.com/EquipCost/Vessel.htmhttp://www.matche.com/EquipCost/Reactor.htm


5/38

+E ,rod'ct and ,rocess esi!$ ,rinciles 2nd Ed Seider

509umps S (gpm+ft1&+2) C-

entri'!al ' GH0.5 e%9.2951:0.6019/C&SI0.05

E3uipment

522Heat Exchanger S (ft1*) C-

S$ell?T'


6/38

Cp

9/C&S2 FT/FM/K

Cp

F/FM/FC/K

FM=aIA100 1."5 3 "0

E;%%& 3."" 3 40

E;%%< 2".3090"44 3 40

0


15/38

0.905"4" 2723."4"77 7402.17""9 1." 13323.922 1""05.6676 36600

0.967032 1637.31267 4750.00124 "550.00223 12067.6554 1300

0.967032 26"0.4"3"4 7776.34093 13997.4137 19756.24"1 35200

0.967032 1992.1377 5779.3"271 10402."""9 146"2."592 2000

0.905"4" 2031.17117 5519.79703 9935.63466 14023.3666 2100

0.905"4" 24"".67537 6763.0"4"3 12173.5527 171"2.011" 3200

96517."0"6

0.967032 1371.31275 397".30994 7160.957"9 10107.12"6 900

0.905"4" 1543.06754 4193.35395 754".0371 10653.4605 1100

0.905"4" 2121.1406 5764.29291 10375.7272 14644.5226 2300

0.9"331" 2920.90364 "616.5313" 15509.7565 21"90."01 52900

*2&00%+20 %0?>&&

0.9"7772 161"0.1969 62539.707 3.17 19"250."71 279"15.506 205900

0.9"396" 9202.07117 29632.2"66 93934.34"7 1325"0.942 1600

+


16/38

o'


17/38

@o+ ump

1 ,:101 27.6" 100 27."" 540 440

2 ,:102 26.7 100 2".44 400 300

3 ,:103 60 400 60.15 540 140

4 ,:104 "0 400 "0.09 540 140

5 ,:105 60 101.3 60.01 120 1".76 ,:106 60.01 110 60.11 250 140

7 ,:107 155 110 155.1 1"0 70

" ,:10" 60 130 60.03 200 70

9 ,:109 6"."5 120 6"."9 190 70

10 ,:110 135.95 140 135.97 1"0 40

11 ,:102/ 2".44 400 2".45 540 140

12 ,:109/ 70 110 70.11 250 140

13 ,:100 94.66 110 94.67 1"0 70

Feed iscocit o'nd


18/38

11 ,:102/ 20.3 0.00390112 20.3056176 1.00545096 46.5334"51

12 ,:109/ 20.3 0.0269421 20.33"7966 0."4127733 55.7052772

13 ,:100 10.15 0.0021721 10.153127" 0.92641551 25.2524957

S = G/H0.5

/H t = ,si0.434 /S

N ensit o Dater at 4de! = 1000-!3 or 62.4 l


19/38

63." 7"3.9 4".9373092 0.5225 0.3373 1.2365924

43.5 1547 96.576116 1.7"7 0."155 2.9"974533

20.3 1124 70.169072 0."195 1.153 4.22707095

20.3 "61.5 53.7"1722 1.713 1.152" 4.22633772

2.7115 "61.3 53.7692364 3."34 0."721 3.1972494220.3 "4".3 52.9576724 4.156 0."546 3.13309179

10.15 776.6 4".4"15"4" 0."106 0."546 3.13309179

10.15 790 49.31"12 0.9121 0.2"15 1.03202123

10.15 73".2 46.0"43496 0.3131 0.2064 0.75669336

5." "91.1 55.629590" 5.109 0.0694 0.254430"1

20.3 1005 62.74014 0."246 0.3306 1.21202919

20.3 "40.9 52.4957052 3.292 0."546 3.13309179

10.15 926 57."0"32" 0.3015 0.260" 0.95613192

t al'es

ump

S M9C

1.2365924 16.930"91 ar


20/38

1.21202919 ".26791246 ar


21/38

269.27 593.74035 0.00316575

746.64 1646.3412 0.012"6225

1015.91 2240.0"155 0.02636726

1015.91 2240.0"155 0.039"673"

764.33 16"5.34765 0.02"07137749." 1653.309 0.0279"14

749." 1653.309 0.022041"4

253.41 55".76905 0.00314"0"

164.21 362.0"305 0.001245"4

"6.0" 1"9."064 0.00056409

330 727.65 0.00390112

749." 1653.309 0.0269421

254.7 561.6135 0.0021721

Motor

,c -# ,c $, AdV'sted ,c

[email protected] 0.05599 0.0750546 1 33".966065 [email protected] 0.05366 0.07193123 1 33".966065 0.9

[email protected]" 0.046"6 0.062"15"3 1 33".966065 0.9

[email protected] 0.06115 0.0"19715" 1 33".966065 0.9

[email protected] 0.006143 0.00"23469 1 33".966065 0.9

1@2"1."1 0.045"3 0.06143512 1 33".966065 0.9

[email protected] 0.02503 0.03355272 1 33".966065 0.9

[email protected]" 0.00"31" 0.0111502" 1 33".966065 0.9

"55.49 0.005767 0.00773066 1 33".966065 0.9

[email protected] 0.001413 0.001"9413 1 33".966065 0.9

Masso5rate(6g#h)

Masso5rate.W(lb#h)

B(psi #

%&&ft)

,*

K* F

T


22/38

965."" 0.01703 0.022"2"72 1 33".966065 0.9

1@2"1.29 0.04623 0.06197132 1 33".966065 0.9

[email protected] 0.00713 0.00955777 1 33".966065 0.9


23/38

ElectricitA

,c -#$

33".97 1@49".19 201.56433".97 [email protected] 193.176

33".97 1@5"3.54 16".696

33".97 [email protected] 220.14

33".97 1@7"5.03 22.114"

33".97 [email protected]" 164.9""

33".97 [email protected] 90.10"


33".97 [email protected] 20.7612

33".97 1@47".70 5.0"6"

,*

Total cost or 'I otor *


24/38

33".97 1@304."5 61.30"



"otal 20@94".21 1369.9"36

3.3

>/.%*/+&=

?%.&>=+?0

-M

CM

(,)(CE in7ex J2&&)

CM

(,)(CE in7ex J 2*0+>)


25/38

Equipment List

E'ient ;te no. escrition

Reactor

Columns Met$anol istillation

FAME ,'rifcation 0.5 W 2.6 H @

Ci'id:li'id E%tractor Sin!le:sta!e Mi%e

Mi%er 0.4 W 1.1

Settler 1.0 W 2.

F+, Settlin! Tan- 1.3 W 2.6 H @

Mixer Feed Tan-

umps

Storage "an6s

Size

D (ft) L (ft)

Reactor Transesterifcation 3.6745406"" 4.4127296655

Columns MeOH distillation 1.32 23

0.4023359994 7.0103999"93

FAME drin! 1.71 ".53

0.5212079992 2.599943996

Mixer Feed 7.61154"56" 9.120734922

2.32 2.7"#as$in! Mi%er 1.15 3.6

0.3505199995 1.09727999"3

&e'trali(ation )S*1000

Separator #as$in! Settler 3.2" 6.6

0.99974399"5 2.0116799969

F+, Settlin! Tan- 4.2653 ".5306

1.30006343" 2.600126"76

Heat Exchanger +E HE% Double ipe 0.00 0

Shell ! "ube 0 00 0

Transesterifcationa 1.2 W 1.4 H @

0.4 W 7 H @ T

2.4 W 2." H @

Heat Exchangersb

a;ncl'des tDo ST+ oerated in series


26/38

ertical clindrical essel@ 100 -!@ S

Settler

H @ ertical clindrical essel@ 910 -!@ S

H @ ertical clindrical essel@ 4000 -!@ S

ertical clindrical essel@ 70 -!@ S

25.026"

Seide E inde%

W (lb) W (t) M9C 9rien+ 4b (ft10) 4 (gal)

1131.07 0.51304472 SSS 350.029722 N 2.7 155902.224

513.044722 1.32500663

3240 1.4696392" SSS 16 235.432914 N 2.7 365393.205

1469.6392" 0."9121053

207.35 0.0940523" S 146.5320"6 N 1 3530".04""

94.0523779 0.5546"42"

1"10 0."2100219 S 3104.32626 N 1 6193".1004

"21.00219 11.75115322020.442 0.9164570" S 27.969"193 N 1 2670".4"64

916.457075 0.105"772"

9000.76" 4.0"2679"7 S 417.141215 N 1 361126.24"

40"2.679"7 1.57905127

154.3235"3 911.73"351 0.002"

3.45130509

0

0

Vac-eted and a!itated ertical clindrical essel@ 520 -!@ 1.4 3@ SSS

o


27/38

215

365.3932

10.029154

33.0"31"4

2."

"0.233234

449.4""46

71.07

Sit$ atches+com

1309.90065 1753.67931 164"00 214649.950249 >ac-eted ? A!itated

233".""167 3131.26679 40700 365393.204733 ol'n@ no internals@edi'

325."92445 436.300906 7700 10029.15422"9 ol'n@ no internals@edi'

1926.07596 257".60745 61600 "0233.233"30" >ac-eted ? A!itated

2107."661 2"21.9"591 25400 330"3.1"40796Mi%erSettler

7176.0629" 9607.22724 : :

2"00 2"00

0 0 0 0 o'


28/38

+E ,rod'ct and ,rocess esi!$ ,rinciles 2nd Ed Seider

509umps S (gpm+ft1&+2)C-

entri'!al ' GH0.5 e%9.2951:0.6019/C

E3uipment

522Heat Exchanger S (ft1*) C-

S$ell?T'


29/38

Storage tan6 S (gal)

Waste 5ater treatment S (gal#min) C-

G Seider Ta


30/38

Cp

SI0.0519/C&S2 FT/FM/K

Cp

F/FM/FC/K

FM=aIA100

values for fob purchase cost

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