m3/h 5~30000 1 ~600 1 ~600 ?? - PowerPoint PPT Presentation

1 / 41
About This Presentation
Title:

m3/h 5~30000 1 ~600 1 ~600 ??

Description:

... Ht.d 5 m.L.C P across rotameter in disch. line + 1 m.L.C dynamic losses in disch. Line ... – PowerPoint PPT presentation

Number of Views:26
Avg rating:3.0/5.0
Slides: 42
Provided by: HN64
Category:
Tags: rotameter

less

Transcript and Presenter's Notes

Title: m3/h 5~30000 1 ~600 1 ~600 ??


1
??? ??????(?)???
  • ?.??
  • 1. ????
  • ???(???)
  • ???
  • ???(???)
  • ???(???)
  • ???
  • ???????(??)

2
m3/h 530000 1 600 1 600
?? m 10 600?? 3 600kg/cm2 3
600kg/cm2 ????? 70
80 6090 15 20
???? ??? ??? ??
?????? ??? ??? ?????
3
?.??????
  • 1. ????????
  • ?? (????)
  • ??
  • ????????
  • ?????

4
2..??????
  • 1)????(?????)
  • 2)????(??????????)
  • 3)????(?????????????)
  • 4)????(?????)

5
3. ?????????
  • 1)??????(????????????
  • ???)?
  • 2)????????
  • 3)????????????
  • 4)???????
  • 5)???????????
  • 6)???????????
  • 7)???????,????????????????

6
(No Transcript)
7

8
???????
9
(No Transcript)
10
(No Transcript)
11
(No Transcript)
12
(No Transcript)
13
Service Hyam reactor feed pump Service Hyam reactor feed pump Item P6705 A/B
Project Z444 PI diagram 6701 Type Centrifugal No.required 2
Liquid Inorganic process liquid Liquid Inorganic process liquid Liquid suction condition Liquid suction condition
Product flow normal
m3/h 69.5 Product flow max
m3/h 77 Density
kg/m3
1219 Viscosity
mPa.s 1.07 Temperature
?
60 Boiling temp.(at atm pressure) ?
110 Boiling temp.(at suction head Hs)
? 111 Flash point
? Crystallisation
?
-5 Contaminated with
Mix with water allowed (for mech. seal)
yes
Pd
Hf.d
Hst.d
Ps
Hst.s
Hf.s
Hd
Hs
14
discharge pressure Pd

2650kPa 221.7 m.L.C.abs discharge static
head Hst.d

27
m.L.C ?P across equipment on disch. side
m.L.C ?P across
disch. Line and valve(s) Ht.d 5
m.L.C ?P across rotameter in disch.
line 1
m.L.C dynamic losses in disch. Line

6 m.L.C ?P across
control valve in disch. Line 83
dyn. losses 5 m.L.C
total discharge head Hd

259.7 m.L.C suction presure Ps
101 kPa 8.4
m.L.C.abs suction static head Hst.s
0.5
m.L.C
8.9
m.L.C ?P across suction line and
valve(s) Hf.s - 0.2
m.L.C

- 8.7
m.L.C.abs

251
m.L.C
15
vapour pressure Pvap
16.3 kpa 1.4
m.L.C.abs N.P.S.H avail. Hs Pvap
8.7 - 1.4 7.3
m.L.C To be checked by contractor when
lay-out is final
16
? ????????? 1 ???? ???????????????????? ?????????
??????????? 2 ???? ???????????????????????????????
?????????????????? 3???? ???????????????????? 4?
??? ????????????
17
?????????????????????? 5???? ?????????????? ????
????(?)?????(?)????kg/h
18
(No Transcript)
19
???.??????????
  • ?. ??
  • . 1. ??
  • ??????
  • (???????)
  • ??????
  • ??????

20
2.? ?
  • ???
  • ??????
  • ???(???)??????????
  • ???????(?????????)????
  • ??????? U???
  • ???
  • ???????
  • ?????
  • ???
  • ???

21
(No Transcript)
22
(No Transcript)
23
(No Transcript)
24
(No Transcript)
25
(No Transcript)
26
?.????????????
27
??? m2/m3 ????? ?????? ??? ???? ???? ?????
????? 40164 ? X X ? X X
U??? 30130 ? X ? ? X ?
??? 35150 ? X ? ? ? ?
?? 2501500 ? ? ? ? ? X
??? 100 ? X ? X X ?
??? 2504370 ? X ? X X X
?? 20 ? ? ? ? ? ?
???? 15 ? X ? ? ? ?
??? 16 ? ? ? ? ? ?
28
2.???????????
  • 1)??????????
  • 2)???????????????
  • 3)???
  • 4)????????????
  • (5)?????????
  • 6)????????????????

29
3.?????????
  • 1)???????????????
  • 2)????????????
  • 3)???????????
  • 4)?????????
  • 5)???????????
  • 6)?????????????????

30
(No Transcript)
31
5.??????????
  • 1)??????
  • ? ?????
  • ???
  • 2)??????
  • ?
  • ??(??)
  • ???

32
6.?????????
  • 1)??????????
  • 2)???????
  • 3)???????
  • 4)?????????

33
7????????????? (1)???????? (2)???? (3)?? (4)?? (5)
????? (6)???? (7)????
34
(No Transcript)
35
? ???????????,????0.4MPa(?),?????F110500kg/h,???
??28,?????F29500kg/h,?????8.0wt,????????37wt,?
????0.2wt,?????W1?10050kg/h,???140?,?????????,???
?????30 ? ,???8??????????????????
F110500kg/h X128
F29500kg/h X28 t2
T2
t130?
W110050kg/h T1140?
36
? 1????? ?????T290?,?????0.2,??????????
Tm(T1T2)/2(90140)/2115? ?????Tm?????
Cp4.24kJ/kg. ? QW1Cp(T1-T2)100504.24
(140-90) 103/3600 5.92 105W 2
??????? ???F2???87 ? tm(8730)/258.5 ?
?tm??? ??Cp10.783KJ/kg. ?, ?Cp24.18kJ/kg.
? CpmCp1.x1Cp2.x20.08 0.7834.18 0.92
3.91kJ/kg. ?
37
t2t1W1.Cp1(T1-T2)/(F2.Cpm) 30100504.18
(140-90)/(9500 3.91) 86.5?
???????,t286.5 ? ??????? ?tm?(140-86.5)(90-
30)?/256.8 ? R(T1-T2)/(t2-t1)(140-90)/(86.5-3
0)0.88 P(t2-t1)/(T1-t1)(86.5-30)/(140-30)0.5
1 ???????0.825 ?tm0.825 56.846.8 ? 3?????
?K700W/m2.K AQ/K ?tm5.92 105/(700
46.8)18.1m2 ??G-400-20-25-4????,??3m,??? 25 2
,???N86,?????150,???Np4
38
4?????? (1)?????????,????????
tm(86.530)/258? F2????? Cp3.91kJ/kg. ?
?0.428cp
?2.244kJ/(m.h. ?) ??????A?/4d2N/Np0.7850.0212
86/40.00744m2 RedG/ ?0.021 9500
103/(0.00744 0.428 3600)1.74 104 PrCp. ?/
?3.6 3.91 0.428/2.2442.68 ?i0.023
?/d.Re0.8Pr0.42622W/(m2. ?) (2)??????
????115 ???? ?947kg/m3 Pr1.54 ?0.243cp
?68. 5 10-2w/(m.k) ???????,???t32mm,25
?????
de0.02m
39
????ABD(1-d0/t)0.150.4(1-25/32)
0.0131m2
???????????,???????Ri ?R0 ??2 10-4m2. ?/w
40
A?Q/(k.?tm)5.92105/(935 46.5)
14m2 A/A?20/141.4
41
?????
  • (1)????????????????????????????
  • (2)????????????(?????)
Write a Comment
User Comments (0)
About PowerShow.com