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Multi-Stage Process and Device for Distributive Production of a Low Sulfur Heavy Marine Fuel Oil

a technology of marine fuel oil and multi-stage process, which is applied in the direction of hydrocarbon oil treatment products, combustion using catalytic materials, physical/chemical process catalysts, etc., can solve the problems of not being able to realize or bring to market the solution for transforming high sulfur hmfo into low sulfur hmfo, and the constraint in the global supply of middle distillate materials, so as to reduce environmental contaminates and minimize the changes in the desirable properties of hm

Inactive Publication Date: 2019-01-03
MAGEMA TECH LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent aims to clean up heavy marine fuel oil by reducing its environmental contaminants in a multi-step process that maintains its useful properties and minimizes the production of unwanted by-products.

Problems solved by technology

Once asphaltenes have precipitated out, they are notoriously difficult to re-dissolve and are described as fuel tank sludge in the marine shipping industry and marine bunker fueling industry.
For over five years there has been a very strong economic incentive to meet the marine industry demands for low sulfur HMFO, however technically viable solutions have not been realized and a premium price has been commanded by refiners to supply a low sulfur HMFO compliant with Annex VI sulfur emissions requirements in the ECA areas.
Notwithstanding this global demand, solutions for transforming high sulfur HMFO into low sulfur HMFO have not been realized or brought to market.
The first major difficulty is the constraint in global supply of middle distillate materials that make up 85-90% vol of MGO and MDO.
It is reported that the effective spare capacity to produce MGO is less than 100 million metric tons per year resulting in an annual shortfall in marine fuel of over 200 million metric tons per year.
Fuel tank sludge causes clogging of filters and separators, transfer pumps and lines, build-up of sludge in storage tanks, sticking of fuel injection pumps, and plugged fuel nozzles.
Such a risk to the primary propulsion system is not acceptable for a ship in the open ocean.
It should further be noted that blending of HMFO with marine distillate products (MGO or MDO) is not economically viable.
The challenge has been that crude oil, distressed oil and residues contain high levels of sulfur, nitrogen, phosphorous, metals (especially vanadium and nickel); asphaltenes and exhibit a propensity to form carbon or coke on the catalyst.
The sulfur and nitrogen molecules are highly refractory and aromatically stable and difficult and expensive to crack or remove.
Vanadium and nickel porphyrins and other metal organic compounds are responsible for catalyst contamination and corrosion problems in the refinery.
Despite the strong governmental and economic incentives and needs of the international marine shipping industry, refiners have little economic reason to address the removal of environmental contaminates from high sulfur HMFOs.

Method used

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  • Multi-Stage Process and Device for Distributive Production of a Low Sulfur Heavy Marine Fuel Oil
  • Multi-Stage Process and Device for Distributive Production of a Low Sulfur Heavy Marine Fuel Oil
  • Multi-Stage Process and Device for Distributive Production of a Low Sulfur Heavy Marine Fuel Oil

Examples

Experimental program
Comparison scheme
Effect test

example 1

Overview:

[0107]The purpose of a pilot test run is to demonstrate that feedstock HMFO can be processed through a reactor loaded with commercially available catalysts at specified conditions to remove environmental contaminates, specifically sulfur and other contaminants from the HMFO to produce a product HMFO that is MARPOL compliant, that is production of a Low Sulfur Heavy Marine Fuel Oil (LS—HMFO) or Ultra-Low Sulfur Heavy Marine Fuel Oil (USL-HMFO).

Pilot Unit Set Up:

[0108]The pilot unit will be set up with two 434 cm3 reactors arranged in series to process the feedstock HMFO. The lead reactor will be loaded with a blend of a commercially available hydrodemetallization (HDM) catalyst and a commercially available hydro-transition (HDT) catalyst. One of skill in the art will appreciate that the HDT catalyst layer may be formed and optimized using a mixture of HDM and HDS catalysts combined with an inert material to achieve the desired intermediate / transition activity levels. The sec...

example 2

MFO

Pilot Unit Set Up:

[0118]A pilot unit was set up as noted above in Example 1 with these changes: the first reactor was loaded with: as the first (upper) layer encountered by the feedstock 70% vol Albemarle KFR 20 series hydrodemetallization catalyst and 30% vol Albemarle KFR 30 series hydro-transition catalyst as the second (lower) layer. The second reactor was loaded with 20% Albemarle KFR 30 series hydrotransition catalyst as the first (upper) layer and 80% vol hydrodesulfurization catalyst as the second (lower) layer. The catalyst was activated by sulfiding the catalyst with dimethyldisulfide (DMDS) in a manner well known to one of skill in the art.

Pilot Unit Operation:

[0119]Upon completion of the activating step, the pilot unit was ready to receive the feedstock HMFO and Activating Gas feed. The Activating Gas was technical grade or better hydrogen gas. The Feedstock HMFO was a commercially available and merchantable ISO 8217 (2017) compliant HMFO, except for a high sulfur con...

example 3

MFO

[0123]The feedstock to the pilot reactor utilized in example 2 above was changed to a commercially available and merchantable ISO 8217 (2017) RMK-500 compliant HMFO, except that it has high environmental contaminates (i.e. sulfur (3.3 wt %)). Other bulk characteristic of the RMK-500 feedstock high sulfur HMFO are provide below:

TABLE 8Analytical Results—Feedstock HMFO (RMK-500)Sulfur Content, mass %3.3Density @ 15° C., kg / m31006Kinematic Viscosity @ 50° C., mm2 / s500

[0124]The mixed Feedstock (RMK-500) HMFO and Activating Gas was provided to the pilot plant at rates and conditions and the resulting sulfur levels achieved in the table below

TABLE 9Process ConditionsHC Feed Nm3 ProductRateH2 / m3(RMK-500)(ml / h),oil / scf TempPressuresulfur Case[LHSV( / h)]H2 / bbl oil(° C. / ° F.)(MPa(g) / psig)% wt.A108.5 [0.25] 640 / 3600377 / 71013.8 / 20000.57B95.5 [0.22]640 / 3600390 / 73513.8 / 20000.41C95.5 [0.22]640 / 3600390 / 73511.7 / 17000.44D95.5 [0.22]640 / 3600393 / 74010.3 / 15000.61E95.5 [0.22]640 / 3600393 / 74017.2 / 25000.3...

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Abstract

A multi-stage process for the distributive production of an ISO8217 compliant Product Heavy Marine Fuel Oil from ISO 8217 compliant Feedstock Heavy Marine Fuel Oil involving a core desulfurizing process that is distributed in a Reaction System composed of multiple reaction vessels. The Product Heavy Marine Fuel Oil has a sulfur level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05 mass % to 1.0 mass. A process plant for conducting the process for conducting the distributive process is disclosed that can utilize a modular reactor vessel contained within a frame work based on ISO 40 foot or ISO 20 foot container dimensions.

Description

BACKGROUND[0001]There are two basic marine fuel types: distillate based marine fuel, also known as Marine Gas Oil (MGO) or Marine Diesel Oil (MDO); and residual based marine fuel, also known as heavy marine fuel oil (HMFO). Distillate based marine fuel both MGO and MDO, comprises petroleum middle distillate fractions separated from crude oil in a refinery via a distillation process. Gasoil (also known as medium diesel) is a petroleum middle distillate in boiling range and viscosity between kerosene (light distillate) and lubricating oil (heavy distillate) containing a mixture of C10 to C19 hydrocarbons. Gasoil (a heavy distillate) is used to heat homes and is used blending with lighter middle distillates as a fuel for heavy equipment such as cranes, bulldozers, generators, bobcats, tractors and combine harvesters. Generally maximizing middle distillate recovery from heavy distillates mixed with petroleum residues is the most economic use of these materials by refiners because they c...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10G65/16B01J23/74B01J21/04B01J23/24B01J23/40B01J8/04B01J8/00
CPCC10G65/16B01J23/74B01J21/04B01J23/24B01J23/40B01J8/0457B01J8/008C10G2300/202C10G2300/205C10G2300/1044C10G2300/302C10G2300/308C10G2300/4062C10G2400/04B01J2208/00557C10L1/04C10G45/04C10G47/02C10G65/12C10G45/00C10G69/02C10L1/12C10L1/14C10L1/1608C10G67/02C10G67/06C10G7/00C10L2200/0438C10L1/183C10G65/04F23C13/08B01D53/18C10G45/22C10G2300/1059C10G45/08C10G25/02C10G25/003B01D3/343B01J8/0492B01J2208/025C10G2300/207C10G2300/30C10G2300/4012C10G2300/4018C10G2300/70C10G2300/80C10L2270/026C10G2300/107C10G2300/1077B01D53/1481C10G45/06C10G2300/1048C10G2400/06C10L2200/0263C10L2270/02C10G45/02C10G2300/208B01J8/0278B01J8/0292B01J2208/02C10G2300/1037C10G2300/201C10G2300/206
Inventor MOORE, MICHAEL JOSEPHKLUSSMANN, BERTRAND RAYWHITE, CARTER JAMES
Owner MAGEMA TECH LLC
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