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Subject: Inquiry
From: DISHA CHEM-FAB LLP <dishachemfab@gmail.com> on Tue, 27 May 2025 12:56:22
To: Manish Tikle <manish@shritara.com>
To,
Shritara Consultant Pvt. Ltd .
K/a :- Mr. Tickle Saheb
Dear sir ,
As per telephonic conversation below is the inquiry for your ref .
We required complete design , Dwg & costing from your end .
Kindly plz provide the same .
As discussed with you, Request you to send the budgetary offer as per blow equipment details :
1) 15 MT EO reactor ( 22 M3 Volume ) Ver cal
a) MOC :316
b) Limpet and inner and EO sparger
c) Agitator type : Pitch Blade Turbine with Maximum speed .
d) Bo om and Top : Dish end
e) Working Pressure 6 Kg/cm2, Design Pressure 8 Kg/cm2
f) No of Nozzles as per your knowledge to be decided at the me finaliza on of design.
g) Working Temperature 220 Deg and Design Temperature 250 Deg C
2) Three no 40 M3 EO storage vessel Horizontal ( Pesho Approved)
a) Two No MOC : SS304 and One MS inside SS 304 cladding
b) Inner Coil for Cooling
c) Side End : Dish End
d) Working Pressure 4 Kg/cm2
e) No of Nozzles as per your knowledge to be decided at the me finaliza on of design.
3) 20 M3 High Pressure Vessel Ver cal
a) Dia :2 M
b) Length : 6.3 M
c) MOC : SS316
d) Thickness of shell : 50 mm
e) Top Dish end Height: 1.2 M
f) Top Dish end thickness : 65 mm
g) Bo om Conical Height : 1.2 M
h) Bo om Conical thickness: 65 mm
i) No of Nozzles to be decided at the me finaliza on of design. And Design pressure to be
considered as per shell thickness
4) 6.5 m3 Melter Ver cal
a) MOC :304
b) Jacket MS
c) Agitator type :Anchor.
d) Bo om and Top : Dish end
e) Working Pressure 1 Kg/cm2
f) No of Nozzles to be decided at the me finaliza on of design.
5) Heat Exchanger area 30 m2
a)Tube MOC SS 304 Shell MOC MS
b) Tube side Ethylene Oxide Flow 12 M3 /Hr
c) Shell side Cooling Water
6)Heat Exchanger area 110 m2 Ver cal
1 of 2 27-05-2025, 13:52
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a)Tube and Shell MOC SS 316
b) Tube side thermic fluid flow 450 m3 /hr inlet temp 60 deg C out let 83.4 Deg C
c) Shell side EO deriva ve : 400 m3/hr inlet temp 180 deg C out let 160Deg C
7)Heat Exchanger area 280 m2 Horizontal
a)Tube and Shell MOC CS
b) Tube side Cooling Water 400 m3 /Hr inlet temp 32 deg C out let 42Deg C
c) Shell side Thermic fluid 450 m3 /hr inlet temp 83.4 deg C out let 60 Deg C
8) Heat Exchanger area 70 m2
a)Tube MOC MS 304 Shell MOC MS
b) Tube side Steam Flow 2500 kg /Hr 450 kg /hr inlet temp 200deg C out let 200Deg C
c) Shell side Thermic fluid 450 m3 /hr inlet temp 153.9 deg C out let 160 Deg C
Your early reply in this regard is highly appreciated.
Thanks & Regards
Disha Chem Fab LLP
Pravin Bhosnle
M. 9820977183
2 of 2 27-05-2025, 13:52
