OMO Plant

OMO Plant

Categorie:

Extra informatie

Merk

SPIE

Type

OMO IPP

Nieuw in

2013

Beschrijving

2013 SPIE OMO IPP riser reactor facility used for production of olefins from methanol (MTO)

General plant information. Also available and with detailed specifications attached in this sale in PDF file. The offered process facility (further called pilot plant) was designed and built for production of Methanol to Olefins (MTO) having a capacity of 3 ton per day. The process is quite similar to FCC, equipped with riser reactors, regenerator, in which the formed coke on the recycled catalyst is burning. This demo/pilot plant is designed and built according to Shell’s DEP, with extensive instrumentations, flexibility for modification and ability to detect and resolve any problem that might arise in production scale plant. This demo plant is for outdoor installation, assembled in modular galvanized steel structure, ATEX compliance, and having control system based on Honeywell process control, separate safety system (ESD), HMI, and Data logging. The plant owner, Shell Technology Center Amsterdam (STCA), has decided to stop further development of this technology and we, our seller is offering this demo plant for sale. Our offered plant is for client use, therefore, not for a specific process and no guarantee for conversion performance. At present, the plant is at storage, consisting of disassembled structures, control and power distribution container and well-stored computers, server and full manufacturing documents. Application summary The offered plant can be used for any process that should be conducted in riser reactor in demo scale. Material of construction of reactors and most of other wetted parts are SS-304, SS316L and the high temperature parts from alloy 625. Possible applications are; Catalyst test and process studies and optimization of; MTO, FCC, catalytic selective oxidation, catalytic cracking/conversion of bio-waste; catalytic dehydrogenation of hydrocarbons. Specification summary; Main riser reactor R-210; total length 23302 mm; upper part 6” sch 80 (ID 146 mm); catalyst flux at normal operating conditions 5,8 kg/m2.s; operating temperature 590 – 610 ºC; design 710 ºC; Second riser R-220; total length 23243 mm; upper part 3” sch 80 (ID 74 mm); catalyst flux at normal operating condition 32,6 kg/m2.s. operating temperature 610 – 623 ºC; design 710 ºC; Regenerator R-230; total volume 0.72 m3; operating temperature 630 ºC; design 710 ºC; Fixed bed reactor for hydrogenation of C4 –C5, R-601; 15 l, Operating press. 20 – 40 barg; Operating temp. 200 ºC; Compressor package X-401; 2 stage; 0.4 – 20 barg; 217 kg/h, medium H2 & N2; SS-316; Dryer package removing water from HCX-451; 619 L gas; Operating; 20 barg; 20 – 170 ºC; Water cooler package X-911; 36564 kg/h; 307 kW cooling; operating temp. 33 – 25 ºC; Water chiller package X-912; 19,6 kW cooling, operating temp. -7 ºC up-to -12 ºC; Fresh catalyst vessel V-260; 450 kg catalyst; Catalyst addition vessel V-254; 10 kg catalyst; E-catalyst receiving vessel V-262; 360 kg catalyst; Bisulfite wash column C-450; 132 L; operating press. & temp.; 5 barg; 53 – 103 ºC; Depropanizer column C-501; 376 L; operating press. & temp. ;10 barg; 15 – 87 ºC; Debutanizer column C-551; 362 L; operating press. & temp.; 5 barg; 53 – 103 ºC; Depentanizer column C-561; 161 L; operating press. & temp.; 1 barg; 55 -125 ºC; The pilot plant is built up from 4 process modules and an incinerator 1. Feed and Reactor and Regeneration unit – R&R (section 2000); 2. Catalyst handling – CH (section 2500); 3. Process module 1 – PM1 (section 3000, 4000, 4500); 4. Process module 2 – PM2 (section 5000 and 6000); 5. Incinerator (section 9000). This module is working independently & it is for sale separately (lot 2). Size and weight; Part I; Reactor, 6.3 x 6.3 x 28.5 meter high, 92 ton weight; Part II; Module I, 12 x 7.5 x 19 meter high, 97 ton weight; Part III ; Module II, 12×7 x 18 meter high, 65 ton weight; Catalyst handling ; 5.5 x 4.5 x 10 meter high, 16 ton weight; Genuine manufacturer of this plant offers its support and services for re-installation and/ or modification of the plant at buyer’s expense. Detailed information is available on request. When plant is sold to buyer, the full technical construction file is transferred to the buyer (on request), available in hardcopy and digitally. Also full 3D plant file and software available, for identification of parts, finding parts and trouble shooting. It is dismantled and stored for sale in Q3 2019 by Mammoet. Mammoet is offering their services for re-installation at buyer’s expense; plant (stored at deep water quay) Beverwijk the Netherlands, Plant Modules Control container, computers & documentations Drachten the Netherlands. Attention international trade control laws, restricted jurisdiction, restricted party applicable.

Downloads:

> Brochure OMO Plant

Beschrijving

2013 SPIE OMO IPP riser reactor facility used for production of olefins from methanol (MTO)

General plant information. Also available and with detailed specifications attached in this sale in PDF file. The offered process facility (further called pilot plant) was designed and built for production of Methanol to Olefins (MTO) having a capacity of 3 ton per day. The process is quite similar to FCC, equipped with riser reactors, regenerator, in which the formed coke on the recycled catalyst is burning. This demo/pilot plant is designed and built according to Shell’s DEP, with extensive instrumentations, flexibility for modification and ability to detect and resolve any problem that might arise in production scale plant. This demo plant is for outdoor installation, assembled in modular galvanized steel structure, ATEX compliance, and having control system based on Honeywell process control, separate safety system (ESD), HMI, and Data logging. The plant owner, Shell Technology Center Amsterdam (STCA), has decided to stop further development of this technology and we, our seller is offering this demo plant for sale. Our offered plant is for client use, therefore, not for a specific process and no guarantee for conversion performance. At present, the plant is at storage, consisting of disassembled structures, control and power distribution container and well-stored computers, server and full manufacturing documents. Application summary The offered plant can be used for any process that should be conducted in riser reactor in demo scale. Material of construction of reactors and most of other wetted parts are SS-304, SS316L and the high temperature parts from alloy 625. Possible applications are; Catalyst test and process studies and optimization of; MTO, FCC, catalytic selective oxidation, catalytic cracking/conversion of bio-waste; catalytic dehydrogenation of hydrocarbons. Specification summary; Main riser reactor R-210; total length 23302 mm; upper part 6” sch 80 (ID 146 mm); catalyst flux at normal operating conditions 5,8 kg/m2.s; operating temperature 590 – 610 ºC; design 710 ºC; Second riser R-220; total length 23243 mm; upper part 3” sch 80 (ID 74 mm); catalyst flux at normal operating condition 32,6 kg/m2.s. operating temperature 610 – 623 ºC; design 710 ºC; Regenerator R-230; total volume 0.72 m3; operating temperature 630 ºC; design 710 ºC; Fixed bed reactor for hydrogenation of C4 –C5, R-601; 15 l, Operating press. 20 – 40 barg; Operating temp. 200 ºC; Compressor package X-401; 2 stage; 0.4 – 20 barg; 217 kg/h, medium H2 & N2; SS-316; Dryer package removing water from HCX-451; 619 L gas; Operating; 20 barg; 20 – 170 ºC; Water cooler package X-911; 36564 kg/h; 307 kW cooling; operating temp. 33 – 25 ºC; Water chiller package X-912; 19,6 kW cooling, operating temp. -7 ºC up-to -12 ºC; Fresh catalyst vessel V-260; 450 kg catalyst; Catalyst addition vessel V-254; 10 kg catalyst; E-catalyst receiving vessel V-262; 360 kg catalyst; Bisulfite wash column C-450; 132 L; operating press. & temp.; 5 barg; 53 – 103 ºC; Depropanizer column C-501; 376 L; operating press. & temp. ;10 barg; 15 – 87 ºC; Debutanizer column C-551; 362 L; operating press. & temp.; 5 barg; 53 – 103 ºC; Depentanizer column C-561; 161 L; operating press. & temp.; 1 barg; 55 -125 ºC; The pilot plant is built up from 4 process modules and an incinerator 1. Feed and Reactor and Regeneration unit – R&R (section 2000); 2. Catalyst handling – CH (section 2500); 3. Process module 1 – PM1 (section 3000, 4000, 4500); 4. Process module 2 – PM2 (section 5000 and 6000); 5. Incinerator (section 9000). This module is working independently & it is for sale separately (lot 2). Size and weight; Part I; Reactor, 6.3 x 6.3 x 28.5 meter high, 92 ton weight; Part II; Module I, 12 x 7.5 x 19 meter high, 97 ton weight; Part III ; Module II, 12×7 x 18 meter high, 65 ton weight; Catalyst handling ; 5.5 x 4.5 x 10 meter high, 16 ton weight; Genuine manufacturer of this plant offers its support and services for re-installation and/ or modification of the plant at buyer’s expense. Detailed information is available on request. When plant is sold to buyer, the full technical construction file is transferred to the buyer (on request), available in hardcopy and digitally. Also full 3D plant file and software available, for identification of parts, finding parts and trouble shooting. It is dismantled and stored for sale in Q3 2019 by Mammoet. Mammoet is offering their services for re-installation at buyer’s expense; plant (stored at deep water quay) Beverwijk the Netherlands, Plant Modules Control container, computers & documentations Drachten the Netherlands. Attention international trade control laws, restricted jurisdiction, restricted party applicable.

Downloads:

> Brochure OMO Plant

Extra informatie

Merk

SPIE

Type

OMO IPP

Nieuw in

2013