Shale Gas Ushers in Ethylene Feed Shifts

December 6, 2018 | Author: Intratec Solutions | Category: Natural Gas, Gas To Liquids, Ethylene, Polyethylene, Methane
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Siluria Technologies

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SHALE GAS USHERS IN ETHYLENE FEED SHIFTS Growth in North American ethane cracking has wider effects for the CPI, while some companies look to harness methane for ethylene

I

ncreasing production of natural gas from hydraulic fracturing of shale deposits has fundamentally altered the landscape of chemical production in North America. The higher margins on steam-cracking steam-cracking ethane to produce ethylene have resulted in significant feedstock shifts in the U.S. over the past two years. Numerous chemical producers are expanding ethylene capacity to take advantage of the increased availability of ethane from natural gas. The shift toward using more ethane as a feedstock for ethylene is generating a number of ripple effects for other chemicals, including tightness in the propylene and butadiene markets. Meanwhile, as manufacturers in energy-intensive industries take advantage of lower energy costs offered by shale gas, other companies continue the pursuit of an alternative route to ethylene using methane as the feedstock. Higher shale-gas production has resulted in a significant and longterm change in the relationship between petroleum and natural gas prices, explains Russell Heinen, director of IHS Chemicals (Englewood, Colo.; www.ihs. www.ihs. com). “This change in price relationships has kept prices for ethane low relative to naptha, which is still the dominant feedstock for ethylene producers worldwide,” he says (Figure 2). IHS is preparing a report, “The Game Has Changed: The Influence of Shale Development on the Global Chemical Industry,” Industry,” to be released rel eased this month. Shale deposits vary greatly in the composition of natural gas. Some areas contain virtually no natural gas liquids (NGLs; ethane, propane

Siluria Technologies has developed a catalyst for the oxidative coupling of methane (OCM), potentially opening the door to commercial-scale ethylene directly from methane in one step

FIGURE 1.

TABLE 1. NORTH AMERICAN ETHYLENE CAPACITY CAPACITY GROWTH Company

Location

Capacity, thousands of ton/yr

Start up year

Dow Chemical Ineos CP Chem Braskem/Idesa Shell Chemical Formosa Plastics LyondellBasell Dow Chemical Williams Westlake Chemical Ineos

Freepor t, Texas Lake Charles, La. Baytown, Tex. Coatzacoalcos, Mexico Pennsylvania Point Comfor t, Tex. Texas and Illinois Hahnville, La. Lake Charles, La. Lake Charles, La. Chocolate Bayou, Tex.

1,906 1,361 1,134 998 90 7 799 658 363 272 104 104

2014–2017 2018 2016–2017 2015 2016+ 2015 2012–2014 2012 (4th Q) 2013 (3rd Q) 2012 2013

Total

8,607 Source: IHS Chemical

and butane), and some are very “wet,” containing from a few percent up to even 20% NGLs. Parts of the Marcellus shale in the eastern U.S. are very wet, for example, notes Heinen, while the Eagle Ford and Barnett shales in Texas produce dryer gas (more methane with less NGLs). Ethane to ethylene Driven by a wide range of derivatives, ethylene is the most-produced organic chemical in the world, with volumes expected to top 160 million tons in 2012, accounting for $150 billion in sales. Major polymers and chemicals made from ethylene include: low-density polyethylene (LDPE); linear lowdensity polyethylene (LLPDE); and high-density polyethylene (HDPE); as well as polyvinyl chloride; ethylene oxide; ethanol; ethylene propylene diene monomer (EPDM) and others. End-use markets include wire and cable insulation; consumer, industrial and agricultural packaging; woven

fabrics; coverings, pipes, conduits and assorted construction materials; drums, bottles and other containers; and antifreeze, solvents and coatings.  According to an analysis by the  American Chemistry Council (ACC; Washington, D.C.; www.americanchemistry.com), the additional output of chemical derivatives generated by a 25% increase in ethane production would translate to $18.3 billion worth of bulk petrochemicals and organic intermediates, intermediates, as well as $13.1 billion worth of plastics resins and $1.0 billion of rubber. New capacity  A major driver of the increasing ethane-cracking capacity is the ratio between crude oil and natural gas g as prices, which has been generally increasing since January 2009, and is at historically high levels (40 to 1 or higher). “To date, most new capacity for ethylene has come through retrofits and expansions, but the bulk of new capac-

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 WIDER SHALE GAS EFFECTS

Newsfront

of additional effects of the shale gas boom is generating profound changes across the chemical industry and beyond, including rising methanol and ammonia production capacity in Athehost U.S., says ACC economist Martha Gilchrist-Moore, who will be speaking about the implica-

tions of the shale gas boom at ChemInnovations 2012, along with IHS’ Heinen (see p. 24D-1). The availability of shale gas will also have a profound effect on manufacturing more generally. Energy-intensive sectors like iron and steel, plastics, glass, rubber, aluminum, fabricated metals and papers all stand to gain from inexpensive shale gas, she says. Also, combined heat and power cogeneration plants are even more economically attractive, she notes.

ity from newly built plants will start to come online in 2016 and 2017,” says IHS’s Heinen. Since 2010, 450,000 ton/yr of ethylene production capacity have been added through retrofits, upgrades and expansions in the U.S., and producers have announced over 5 million ton/yr of new ethylene capacity that are scheduled to come online by 2018 (Table 1). And since the additional ethane potential would allow about 11 million ton/yr of ethylene, there is still plenty of room for new capacity to be added to balance potential supply with demands. That means more ethylene capacity is likely, Heinen says. Industry faces several challenges associated with the added capacity, Heinen notes, including the ability to bring capacity online without delay, and the ability of ethylene producers to work out the supply logistics of handling nearly 300–400 thousand bbl/d of new ethane by 2020. Also, Heinen points out that other potential challenges are that U.S. ethylene supply increases could impact pricing; and environmental concerns related to shale-gas drilling could spur legislation restricting hydraulic fracturing.  Another challenge for ethylene producers is that some of the newer crackers are ethane-specific, giving up feedstock flexibility to focus on ethane cracking, so future growth might be hindered if economics change and flexibility is needed.

notes Felipe Tavares, director of Intratec (Houston; www.intratec.com). Several on-purpose propylene production alternatives exist, including those using NGLs — propane dehydrogenation (PDH) and propylene production  via metathesis chemistry. PDH is a catalytic process in which the hydrogen byproduct can be used as fuel for the reaction. Metathesis is a catalyzed reaction between butenes and ethylene where double bonds are reformed. Propylene technology is among the first topics covered in Intratec’s “Knowledge Base,” an online encyclopedia of chemical technology and economics. The tool can be found at: base.intratech.us. Capacity growth for propylene from PDH is poised to grow significantly. The Dow Chemical Co. (Midland, Mich.; www.dow.com) has announced plans for a 750,000 ton/yr PDH plant in Freeport, Tex., using technology from UOP LLC (Des Plaines, Ill.; www. uop.com). Formosa Plastics and Enterprise Products Partners LP (Houston; www.enterpriseproducts.com) has also announced plans for PDH facilities on the U.S. Gulf Coast. Lummus Technology / CB&I Co. (The Hague, the Netherlands; www.cbi.com) is currently the only licensor to offer an olefin metathesis process, known On-purpose propylene as olefin conversion technology (OCT), The shift to lighter feedstocks for eth- to make propylene from ethylene and ylene (using more ethane) is beginning butenes. In cases where only ethylene to have ripple effects that are likely is readily available, Intratec’s Tavares to grow going forward. When steam- says the metathesis process could be cracking naptha or gas oil, propylene combined with a dimerization plant, and other chemicals are formed as which converts ethylene to 2-butene. co-products alongside ethylene; but when ethane is the feedstock, ethyl- Utilizing methane ene is the primary product, with mini- While methane from natural gas will mal co-products formed. So the shift to continue to play a prominent role as ethane as a feedstock has resulted in a cleaner-burning alternative to coal tighter supplies of three- and four-car- for power generation, its abundance bon chemicals, particularly propylene (~10 times more than ethane in natuand butadiene, which is likely to raise ral gas) and price (about half the price prices for those chemicals, says IHS’ of ethane) is spurring a wide-ranging Heinan (Figure 3). effort to utilize methane directly as Tightness in propylene supply has a feedstock for ethylene and other improved the cost-competitiveness chemicals, rather than burning it as of on-purpose propylene production, fuel (Figure 1). Since so much natu18

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ral gas is available, new demands for methane are needed, says Rahul Iyer, senior director of corporate development at Siluria Technologies (San Francisco, Calif.; www.siluria.com). Dallas Kachan (Kachan & Co.; San Francisco, Calif.; www.kachan.com), an analyst and consultant in the clean technology industry, points out that the energy and capital intensity required for steam cracking of ethane provides an incentive to make ethylene in alternative ways. Commercially  viable ways to make ethylene directly from methane, if successful, could be a watershed moment for the chemical and petroleum industries, Kachan recently wrote in a blog post. Significant activity is ongoing toward commercialization of methaneto-ethylene technologies, with many startups — some announced and some “undercover” — working on various technologies, while university and government laboratories also attack the problem, according to research by Kachan & Co. The major integrated petroleum companies, including Chevron, ExxonMobil, Shell and BP hold a surprisingly wide-ranging portfolio of patents for methane-to-ethylene technologies, and several large chemical companies also hold some intellectual property in this area (BASF, Lubrizol, SABIC, GE, Honeywell and others), Kachan research found. Methane-to-ethylene technologies are being considered for use in remote areas where natural gas associated with crude oil drilling is flared, or remote gasfields where no pipelines exist and transporting the gas is difficult. Smaller-scale gas-to-liquids (GTL) technologies are needed for areas with “stranded gas,” says Sulkhan Davitadze, an investment director at Bright Capital (Moscow, Russia; www. bright-capital.com), a venture capital firm with a portfolio of companies in the energy and chemicals areas.  A number of smaller-scale GTL processes exist, some using a FischerTropsch (F-T)-based approach and some taking different paths. All are

 S   y n F   u  e l    s  I   n  t   e r  n  a  t  i    o n  a l  

Source: IHS Chemical

U.S. ethylene production by feedstock  30,000 25,000   s 20,000   n   o    t   c    i   r 15,000    t   e    M

10,000 Heavier Butane

5,000 0

        0         9         9         1

        1         9         9         1

        2         9         9         1

        3         9         9         1

        4         9         9         1

       5         9         9         1

        6         9         9         1

       7         9         9         1

        8         9         9         1

        9         9         9         1

        0         0         0         2

        1         0         0         2

        2         0         0         2

        3         0         0         2

        4         0         0         2

       5         0         0         2

        6         0         0         2

       7         0         0         2

        8         0         0         2

Propane Ethane

        9         0         0         2

        0         1         0         2

        1         1         0         2

        2         1         0         2

Shale gas has pushed natural gas and ethane production higher. Forecasts indicate the production will rise further FIGURE 2.

Source: IHS Chemical

33

Steam cracker propylene and butadiene production Ratio to ethylene

8

31

8

   %29  ,   e   n   e 27    l   y    h    t 25   e    /   e   n 23   e    l   y 21   p   o   r    P 19

Propylene/ethylene

17

Butadiene/ethylene

7 7 6 6

15

5

   %  ,   e   n   e    l   y    h    t   e    /   e   n   e    i    d   a    t   u    B

5

   0    1    2    3    4    5    6    7    8    9    0    1    2    3    4    5    6    7    8    9    0    1    2    1    1    9    9    9    9    9    9    9    9    9    9    0    0    0    0    0    0    0    0    0    0    1    0    0    9    9    9    9    9    9    9    9    9    9    0    0    0    0    0    0    0    0    0    0    0    1    1    1    1    1    1    1    1    1    1    2    2    2    2    2    2    2    2    2    2    2    2    2

4

Propylene and butadiene production (shown as a ratio to ethylene) have fallen as a result of the shift to lighter feedstocks by ethylene producers FIGURE 3.

potentially useful, but it’s not clear yet what the economics will turn out to be, Davitadze remarks. SynFuels International (Dallas, Tex.; www.synfuels.com) is looking to make higher-value chemicals from methane without using Fischer-Tropsch chemisty. SynFuels has designed a non-catalytic, water-jacketed, fixedbed reactor that pyrolyzes methane, generating a mixture of gases composed mostly of acetylene, as well as some carbon monoxide and hydrogen (Figure 4). The gas mix is fed into an absorber that separates the acetylene from the other gases.  Acetylene is then hydrogenated, while still absorbed, using some of the hydrogen produced in the initial pyrolysis step. A specially designed hydrogenation catalyst that tolerates high levels of carbon monoxide is used. The process, based on technology originally conceived at Texas A&M University (College Station, Tex.; www.tamu.edu), is capable of producing polymer-grade ethylene in 96% yields from acetylene. The ethylene can also be taken further to gasoline blendstock (a mix of C4 to C12  hydrocarbons) through an oligomerization technique also devel-

oped by SynFuels. The company operates a fully integrated GTL demonstration plant in Bryan, Tex., capable of processing 50,000 ft 3 /day of natural gas into gasoline blendstock. Siluria Technologies is trying to commercialize a single-step methaneto-ethylene process. The company just announced plans to build a demonstration facility for its process, which is based on oxidative coupling of methane (OCM) chemistry. According to Siluria CEO Alex Tchachenko, construction on the demonstration plant will begin in 2013, and it will be capable of producing hundreds of thousands of gallons per year. Siluria’s technology depends on a carefully made catalyst that promotes ethylene formation over non-selective oxidation reactions (Chem. Eng., December 2010, p. 12). Siluria’s technology is attractive because it’s a one-step process that is capital efficient as well as energy efficient, Davitadze comments. Using a genetically engineered bacteriophage (bacteria-infecting virus) as a template for material growth, Siluria scientists developed a catalyst material that has a unique crystal structure and surface morphology. The structure

FIGURE 4.  SynFuels

International uses methane in pyrolysis reactors to generate acetylene, which is then hydrogenated to ethylene

gives rise to catalyst active sites that can select ethylene formation over non-specific oxidation of methane. The catalyst is a doped metal oxide of transition metals that is designed for compatability with existing petrochemicalindustry infrastructure. The Siluria technology has a number of advantages over F-T approaches because it can be accomplished in one step, at lower temperatures, and works well with existing hydrocarbon processing equipment. Siluria’s OCM technology is an exothermic reaction, so it requires less energy input, and the heat given off by the process can be harvested to drive the process. “We believe we are the first to develop a commercially viable, scalable process for OCM,” Tchachenko says. Siluria’s catalyst-discovery engine has the potential to develop other catalysts to make different products. Siluria’s Iyer says the company will be able to achieve the economics enjoyed by a world-scale plant in a much smaller facility, so significant capital-expense savings are possible. OCM is also of interest to the Polish national research laboratory Fertilizer Research Institute (Pulawy, Poland; www.ins.pulawy.pl). Scientists there have built a pilot plant for a methane-to-ethylene facility based on OCM. Also, UOP has reportedly proved, in the laboratory, a one-step process for directly converting methane to ethylene. The company is looking for partners to build a pilot plant for the process. UOP says its technology could potentially save 40% of the ■ cost of ethane-based ethylene. Scott Jenkins Editor’s note:

An expanded version of this article, with additional background information and graphics can be found at www.che.com.

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