economics

mira misao

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Nov 28, 2013, 10:37:35 AM11/28/13

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Salam

boleh tak sesiapa tolong listkan equipment used in our plant and berapa banyak? nk buat economic. plssss.

Mason W.

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Nov 28, 2013, 11:11:34 AM11/28/13

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On Thu, Nov 28, 2013 at 11:37 PM, mira misao <mira....@gmail.com> wrote:

Salam

boleh tak sesiapa tolong listkan equipment used in our plant and berapa banyak? nk buat economic. plssss.

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List.docx

mira misao

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Nov 28, 2013, 2:11:22 PM11/28/13

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korang, pls reply here ur dimensions of the reactor.

height, length, area , diameter. reply asap k. esok pg ke.

mira misao

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Nov 28, 2013, 2:25:58 PM11/28/13

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height, length, area , diameter. volume reactor.

kalau spe2 dapat utk pump, heat exchanger, condenser, compressor, bg skali k. need those data. sorry kalau kacau. hehe need help for completing the economics part.

mira misao

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Nov 29, 2013, 8:20:18 AM11/29/13

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haii. saya nk start buat keje ni. meh la bg dimensions.

Amalia Hussin

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Nov 29, 2013, 8:23:40 AM11/29/13

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ammonia converter

height = 11 m

tube length = 10 m

bed area = 12.75 m2

diameter = 4.0291 m (outside)

inside diameter = 3.8251 m

misao buat part yg mana? orang kena sambung yg mana ni.

mira misao

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Nov 29, 2013, 8:26:54 AM11/29/13

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kak ya da siap kn ke hazop kak ya? aritu xsiap lg kan? siapkn tu dulu.

Mason W.

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Nov 29, 2013, 8:45:33 AM11/29/13

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Lupa pula

Urea reactor

Volume: 150m3

Height : 14m

No. of Trays : 15

Operating Pressure : 150atm

Design Pressure : 175atm

Operating Temperature : 180°C

Design Metal Temperature : 250°C

Material: Low Alloy Carbon Steel

Prilling Tower

Volume 160m3

Height: 13m

Surface area: 15m2

Material: Carbon Steel

My HE:

Area : 2200ft2

Pressure: 150 psi rating

Material: Carbon steel

mira misao

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Nov 29, 2013, 10:39:03 AM11/29/13

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Please cooperate. I have a lot of things to do. and i'm just estimate the equipment price such as separator, cooler, compressor, to be truth i didnt expert in estimating n the economics things. so pls i just need ur reactor dimensions.

Mohammad Taufik Ibrahim

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Nov 29, 2013, 11:13:10 AM11/29/13

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Ya Allah misao maaf ak lmbt dpt email ni.

Jap2 ak bukak kat pc.

Mohammad Taufik Ibrahim

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Nov 29, 2013, 11:18:57 AM11/29/13

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HTS LTS

Therefore, total height of reactor = height of closures + tube length

= 2(1.5) + 16.914

= 19.914 m

Volume of dish, V = 0.0847 D_i³

= 0.56 m³

D_i = internal diameter = 1.875 m

f = Design stress = 1.18 x 10⁸ N/mm²

Design Pressure, P_d = 1.05 x 3161 = 3319.64 kPa 3320 kPa lebih kurang 33.20 atm

Total volume of reactor = 46.68 m³

--

Yakin bahawa esok akan jadi lebih baik......

MOHAMMAD TAUFIK BIN IBRAHIM

CHEMICAL ENGINEERING

13149

Mohammad Taufik Ibrahim

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Nov 29, 2013, 11:19:40 AM11/29/13

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terlupa

Area of bed, A_b = V_v/v_s

= 2.76 m²

mira misao

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Nov 29, 2013, 1:47:31 PM11/29/13

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one more thing. semua yg reactor yg gune catalyst. boleh bagi berapa mass catalyst korang gune? n nama catalyst. price da ada. nak mass je.

Mohammad Taufik Ibrahim

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Nov 29, 2013, 1:48:21 PM11/29/13

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Ok jap. Ak tgh makan satgi ak bagi.

Mohammad Taufik Ibrahim

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Nov 29, 2013, 2:55:29 PM11/29/13

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iron oxide
60,600.01 kg.

Amalia Hussin

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Nov 29, 2013, 7:31:20 PM11/29/13

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iron oxide = 190 641 kg

Mohd Nizar Mohd Nasir

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Nov 30, 2013, 1:03:41 AM11/30/13

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sorry sgt2 lambat.

height :7.096m

Di: 3.5936m

Do: 3.6576

reactor volume: 9.72m3

Volume catalyst bed: 4.86m3

catalyst weight: 2674.19kg

catalyst : nickel oxide

Best Regards,

Nizar Nasir
Final Year Final Semester

Chemical Engineering

Universiti Teknologi PETRONAS

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