Giving the Old Chrome Catalyst New Life

The SPE’s annual Polyolefins conference in Houston is always a good place to look for catalyst news, and this year is no exception. Polyolefins 2012, held February 26-29 at the Hilton Houston North Hotel (www.spe-stx.org/conference.php), includes a presentation on an advance in control of long chain branching with a very traditional catalyst—chromium. Eric Schwerdtfeger, senior research chemist at Chevron Philips Research Center in Bartlesville, Okla. (www.cpchem.com), will present a patent pending new highly long-chain-branched HDPE made by a new variation of Phillips’ chromium on silica catalyst.

At the Polyolefins Conference, Chevron Phillips will present work on a new chromium catalyst for HDPE that controls long chain branching, a trick normally done with LDPE using metallocene catalysts. This chart shows that the new catalyst produces more LCB with lower concentrations of ethylene in the reactor.

Chromium catalysts are known for making HDPE with broad molecular weight distributions (MWD) and a high molecular weight tail of long linear chains, but low levels of long chain branching–much, much lower than in  LDPE, for example. Broad MWD and long linear chains are needed for strength, especially against stress cracking. Long chain branches, which create Y-shaped chains, are generally bad for physical properties, but help processability.

This modified chromium catalyst is different because it can control production of long chain branching even on HDPE. In fact, it can dramatically increase the frequency of LCB to more than 40 per million total carbon atoms vs. only a fractional amount per million in HDPE normally, Schwerdtfeger says. Even at ppm levels LCB improve processability and melt strength, reduce sag and prevent ovality in large diameter pipe, improve shear thinning, and reduce die swell, Schwerdtfeger adds.

The catalyst research team, headed by Max McDaniel, a senior fellow at Chevron Phillips, used an advanced research tool, known as SEC-MALS (size exclusion chromatography coupled to multi-angle light scattering) with its chromium catalyst to determine the location of long chain branches within the MWD. MALS measures radius of gyration, or the “size” of a molecule, by passing laser light at different angles through a column of molecules in solution. Combined with size exclusion chromatography (SEC), also known as gel-permeation chromatography, it shows where long chain branches are concentrated in the molecular weight peaks of the polymer.

Early inventors at Phillips celebrate the 35th anniversary of inventor Max McDaniel two years ago. From left, Don Norwood invented the slurry loop reactor; Marvin Johnson invented refining catalysts; Paul Hogan co-invented chromium on silica catalyst; Joe Shveima invented chromium on silica catalyst for HMW film; and McDaniel invented some 350 patents including the highly significant SSA cocatalyst for metallocenes.

At the Polyolefins Conference, a younger inventor at Chevron Phillips, Eric Schwerdtfeger, will present their latest development in chromium catalyst technology with controlled long chain branching, allowing high levels of LCB in HDPE for the first time.

Polymer chains with long chain branches “occupy a smaller volume in solution than do linear chains of the same MW. SEC-MALS measures the average size of solvated molecules. It has allowed us to see for the first time the placement of LCB within the MW distribution,” McDaniel writes in a technical paper on the same work to be published in the “Journal of Polymer Science Part A: Polymer Chemistry.” SEC-MALS was used previously to measure long chain branching in metallocene polymers, but this is believed to be its first use with a chromium catalyst.

“Max has unlocked the nature of the chromium catalyst and how it relates to long chain branching,” explains Michael Jensen, a senior scientist at Grace Davison Specialty Catalysts, Columbia, Md. (www.grace.com), which develops catalysts with Chevron Phillips and other resin producers. “Typically with a chromium on silica catalyst, the way to control long chain branching (in the polymer) is through tailoring and treating the silica support. Now Chevron Phillips can create either a very low or very high level of long chain branching with traditional Phillips catalyst. Before, trying to tune long chain branch formation was primarily empirical.” This highly chain branched HDPE has only been produced in a lab scale reactor so far, but the technology is expected to be applicable to Phillips loop reactors. Higher levels of control of long chain branching in HDPE has potential for large diameter pipe, geomembrane, and some types of blow molding.

Chevron Phillips has already used a chromium catalyst with LCB manipulation to make two PE100 pipe resins (H524 and H525) since 2003 and 2004 respectively. PE100 pressure pipe resins are generally bimodal or have broad MWD to meet high performance requirements with good processability. They typically contain long linear molecule chains, which span more amorphous regions in the polymer than Y-shaped long chain branches of the same molecular weight. PE100 is a European ISO standard for pipe resins, rated to hold 100 bar of pressure at 20 degrees C. The U.S. pipe standard is ASTM 4710 with PN (pressure nominal) grades up to PN 16 for pipe, rated for a maximum pressure of 16 bar.

BIMODAL HDPE IN A SINGLE LOOP REACTOR

Very tight control of molecular chain development is usually associated with metallocene catalysts and narrow MWD polymers, not with chromium catalyst and broad MWD polymers. But McDaniel, who doesn’t use the title of doctor if he can help it and is seldom listed first on some 350 patents with his name, holds major patents in both catalyst groups. McDaniel has worked 37 years at Phillips, starting out under Paul Hogan and Robert Banks, the original inventors of the chromium catalyst for PP and HDPE. So it’s fitting that he should be the one to update the chromium franchise.

On the metallocene catalyst side, McDaniel’s research team also recently developed single-reactor bimodal HDPE technology (U.S. Pat. # 7619047 in 2009; U.S. Pat. Applic. # 20110201770 in 2011). This technology uses a dual-metallocene catalyst with Phillips SSA (solid super acid) activator and can also create broad MWD bimodal or multi-modal HDPE in a single Phillips loop reactor.

Chevron Phillips in this mLLDPE packaging film controls strength properties with metallocene catalysts. Now Phillips traditional chromium catalyst can have similar control of long chain branching in broad MWD HDPE. Potential markets include large diameter pipe, shown with Chevron Phillips technical service engineer Pam Maeger.

Chevron Phillips, however, isn’t the first company with a single-reactor bimodal. Univation Technologies LLC in Houston, Texas (www.univation.com), a joint venture between ExxonMobil Corp. in Texas (www.exxonmobil.com), and Dow Chemical Co., Midland, Mich. (www.dow.com), launched its “Prodigy” metallocene catalyst technology for bimodal HDPE made in a single gas-phase reactor in 2007.

But Chevron Phillips’s bimodal catalyst technology may offer more real-time flexibility because Chevron Phillips’s SSA cocatalyst system is formulated on site. “The CPChem activator supports are a real breakthrough for single-reactor bimodals,” says Kenneth Sinclair, principle of polyolefin research firm STA*Research, Foothill Ranch, Calif. (staresearch@juno.com). “With the activator support you can prepare the catalyst in line as you are feeding the reactor and tailor MWD dynamically.”

The single reactor bimodal technology may become available to Phillips licensees, but only with an additional fee. Philips licensees account for about 40% of global HDPE production capacity, according to Chevron Phillips, so the licensing potential could be enormous.

The SSA activator, or cocatalyst, was invented by McDaniel and Grace’s Jensen over a decade ago, and was the first low-cost support/activator for metallocene resins. (McDaniel and Jensen won Phillips’s Shield Innovation Awards for it 1999.) The SSA cocatalyst can make the total metallocene catalyst package significantly less expensive than the traditional metallocene package with MAO (methylalumoxane) or boron as cocatalyst, which are used in many commercial metallocene polymers. Cocatalyst is a big cost item, since anywhere from 100:1 up to 1000:1 or more of it is used than of metallocene, and that doesn’t count the silica that may be used to support the cocatalyst.

The acronym SSA, by the way, is fuzzy. Originally it stood for “solid super acid,” a chemically treated solid oxide used in petrochemical cracking, but not in polymer production before. SSA in polymer production has come to stand for “supported” or “solid single-site activator” or “solid support activator.”  There are almost 100 Chevron Phillips patents involved, starting with a Patent Cooperation Treaty in 1999. Three significant patents are U.S. Pat. # 6239059 in 2001; U.S. Pat. #6613852 in 2003; and U.S. Patent # 7148298 in 2006.

SSA isn’t the only way to reduce the total cost for metallocenes anymore either. In 2008, Albemarle Corp., Baton Rouge, La. (www.albemarle.com), introduced its ActivCat activation technology, which reportedly doubles the activity of silica-supported metallocenes used with MAO cocatalyst. Raghu Menon, business development manager, performance catalyst solutions at Albemarle, will present an update at the Polyolefins conference on “Albemarle’s ActivCat Activation Technology that Enables Polyolefin Producers to adopt Metallocene Catalysts.”

Other polymer companies are also working on developments in support activators for metallocenes for both HDPE and PP: Total Petrochemicals in Brussels, Belgium (www.totalpetrochemicals.com) for HDPE and Lummus Technology (part of CB&I Chicago Bridge and Iron Co.) in The Woodlands, Texas (www.cbi.com); ExxonMobil; and Sumitomo Chemical in Japan (www.sumitomo-chem.co.jp) for PP, says STA*Research’s Sinclair.

A PLACE IN CATALYST HISTORY

McDaniel’s SSA cocatalyst technologies may have played a significant role in allowing Phillips to negotiate a settlement with ExxonMobil after prolonged patent infringement lawsuits. Throughout the 1990s, Exxon aggressively defended several patents, especially the “’800 patent” (U.S. Pat. # 5324800 in 1991 issued to Howard Welborn Jr. and John Ewen for a “Process and catalyst for polyolefin density and molecular weight control”). The ‘800 patent covers a substituted bis-cyclopentadiene metallocene catalyst with MAO cocatalyst.

Exxon sued Mobil in late ’96 on the basis of the ‘800 patent and won its metallocene patent infringement suit in 1998, when a federal court in Texas ordered Mobil to pay $171 million to Exxon. Instead, the two companies signed an agreement to merge, which they did in 1999, forming the biggest company in the world at the time. Dow and Exxon, whose historic patents (on mono-cyclopentadiene metallocene catalysts) were applied for and issued within a few days of each other, settled their disputes in 1999.

Shortly after winning the judgement against Mobil, Exxon sued Phillips in 1998, also on the basis of the ‘800 patent. Phillips won the first round on a technicality without going to trial. Exxon appealed and the appellate court ruled in Exxon’s favor and ordered a trial. In October 2001, before the case went to trial, the two companies announced that they had cross-licensed each other’s technologies. Exactly what metallocene technology Chevron Phillips Chemical licensed ExxonMobil is confidential, but a big part of the settlement is believed to have been McDaniel’s SSA cocatalyst inventions.

There are probably fewer than a dozen inventors of truly major polyolefin catalysts and cocatalysts. Hogan and Banks for the chromium catalyst for PE and PP; Karl Ziegler and Giulio Natta for the titanium catalyst for PE and PP; Walter Kaminsky and John Ewen for the alumoxane cocatalyst for metallocene for PP and PE; and the unassuming inventor Max McDaniel for the SSA cocatalyst for metallocenes.

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High Noon for Small High-Barrier Gas Tanks

New nano barrier materials are finally stepping up to meet the challenge of permeation standards for the gas tanks for golf carts, snow mobiles, boats, lawn mowers and other recreational equipment. The standards from CARB, California’s Air Resources Board, and the U.S. Environmental Protection Agency shouldn’t have taken the recreational vehicle industry by surprise. The first regulation passed in California nearly 10 years ago, but starting January 1, the California limits get a lot tougher.

From 2007 through 2011, CARB phased in permeation limits of 2.5 g/m2/day for different off-road engine sizes. In 2012-2013 CARB’s permeation limits will drop to only 1.5 g/m2/day at 40 degrees C—considerably tougher than EPA limits. On January 1, CARB’s new permeation level will apply to tanks for equipment with >80 to <225 cc engines and in 2013 to tanks for engines over 225 cc.

‘INNOVATIVE’ GAS TANKS APPROVED BY CARB

If CARB in California issues an Executive Order approving a barrier gas tank design, any tank made the same way complies in California. The EPA also certifies tanks by design, but EPA certified tanks still need permeation testing in California. 

Manufacturer              Executive Order            Tank Description

Arkema Inc.                C-U-05-005                    PetroSeal rotomolded fuel tank

Centro Inc.                  C-U-06-027                    “P” family fuel tanks w/ barrier layer

Centro Inc.                  C-U-06-028A                 “Q” family fuel tanks w/ barrier layer

Centro Inc.                  C-U-06-029                    “R” family fuel tanks w/ barrier layer

GE Plastics                 C-U-07-007                      Xenoy 6620U-1001GT or Xenoy 6620-

(SABIC Innovative     (C-U-07-007a)               BK1066GT injection molded fuel Tank Plastics)

Cyclics Corp.              Q-08-001                          CBT injection molded fuel tank

SABIC Innovative      Q-08-006                         Xenoy X6800BM-1001, Plastics                                                                    BK1066, Xenoy X6800BM-RD6D122     

Arkema Inc.                Q-08-012                         “One Shot” Petroseal for California Phase II

Solvay Advanced        Q-08-025                         Ixef BXT-2000 Polyarylamide (PARA) for Polymers LLC                                                        CE 10 test fuel

Centro Inc.                  Q-08-027                          Roto LO Perm material for CE 10 test fuel

Centro Inc.                  Q-08-027a                        Roto LO Perm with XLPE material for CE

Custom Resins            Q-08-028                         Nylene 494 BLK for Calif. Phase II fuel

LG Chem America     Q-08-041                          Hyperier-IP-1105 for Calif. Phase II fuel

LG Chem America     Q-11-017                           Hyperier-IP-1106 for natural & colored

LG Chem America     Q-11-020                         Hyperier-IP-1106 for black blow molded

Source: CARB

The EPA started regulating gas tanks for RVs in 2008, added hand-held “spark-ignited” engines in 2009 for models already certified in California and 2010 for all other models. The EPA added tanks for engines over 225 cc like ride mowers and portable marine tanks in 2011 and will add tanks for engines under 225 cc and installed marine tanks in 2012. But the EPA standards are only <1.5 g/m2/day at 28 degrees C or <2.5 g/m2/day at 40 degrees C. (Permeation rate generally doubles for every 10 degree rise in temperature.)

California approves gas tank barrier construction by “executive order.” Between 2006 and 2009 California approved an average of 10 barrier fuel tank constructions a year; none in 2010; and six in 2011. Confusingly, some tanks were tested with regular gasoline (Phase II California Reformulated Certification fuel) and some with 10% ethanol (E10 fuel). The EPA certifies tanks by design, but EPA certified tanks still need permeation testing in California.

The timing for a sweeping, somewhat confusing and inconsistent revision of small gas tank production was unfortunate, coming with a recession. “OEMs initially tried to fight the regulations, and then were behind the 8 ball on compliance,” notes one material supplier to the small tank market. Some gas tanks already complied. Small lawn mower tanks injection molded out of nylon in two halves and welded together met the permeation limits. But many larger gas tanks of diverse shapes were blow molded or rotationally molded out of HDPE, with no barrier.

Five years ago the choices for blow molded tanks to meet the new barrier standards were limited to six-layer coextrusion with EVOH or off-site barrier treatment with fluorination or sulfonation. Six-layer coex, the gas tank pioneered by the auto industry 20 years ago, is a wonderful barrier, but wasn’t considered economical for parts with low annual production. Fluorination and sulfonation add cost and transportation and don’t hold up well in durable applications.

Another possible solution was new nano barrier materials. Several were presented at the SPE Annual Blow Molding Conferences and at marine and outdoor equipment conferences, but they were untried. The big market for barrier materials has always been food packaging, which has very different requirements. It doesn’t have to contain VOCs under high pressure through cold temperature drop tests.

Finally at SPE’s Annual Blow Molding Conference last October 12-13 in Chicago (www.blowmoldingdivision.com), the first successes with the new barriers appeared. Industrial blow molder Mergon Corp. of Anderson, S.C. (www.mergon.com), presented “Alternative Solutions for Barrier Materials,” a remarkable  report of processing experience with five new barrier materials.  Mergon, which specializes in short production runs across a broad size range of 1- 60 liter blow molded parts, conducted up to three years of Design of Experiments tests on the new materials, solved processing problems, developed new quality control procedures, and qualified some for production. Mergon’s report is also the first public mention of some of the new materials themselves.

NANO, NANO

In 2007 Mergon began testing Hyperier (hyper barrier), a nano barrier made by LG Chem Ltd. in Korea with U.S. offices in Englewood Cliffs, N.J. (www.lgchem.com). Introduced at NPE 2006, Hyperier is a composite of nylon with exfoliated Montmorillonite clay platelets with an aspect ratio of 200-300, compatiblized with HDPE for blow molding. It’s blended into monolayer HDPE tanks at loadings of 16% to 24% to meet both the EPA and new CARB permeation limits. Mergon worked with Hyperier for four years, solving numerous problems, and can run Hyperier on both continuous extrusion and accumulator head blow molding machines with different set points, but without modification of machine or extrusion screws.

Blow molder Mergon blends Hyperier, a new nano barrier material, into monolayer HDPE gas tanks for high barrier. On startup the first six parts are scrapped. Before the barrier mixture reaches the right temperature, nylon-based pellets are visible in the HDPE.

Melt temperatures and pressures have to be very tightly controlled and alarmed, Mergon found.  “You have to overheat the HDPE and under heat the Hyperier,” says Steve Thompson, engineering specialist at Mergon. “Hyperier has to be heated to where the nylon starts to break down, or it doesn’t mix properly. If it’s heated too much, the barrier breaks down. Plus or minus 5 degrees C makes the difference between very good, good, or poor barrier. If you hit an alarm, you have a breakdown in barrier.”  Mergon scraps the first six parts on startup while temperature and pressure come under control. Mergon tests barrier in production every two hours by cutting a tank open, measuring wall thickness, and physically measuring and counting the nano stripes. California Executive Order Q-11-017, approving fuel tanks made with Hyperier IP1106, requires a minimum barrier thickness of 1.8 mm with a nominal wall thickness of 2.8 mm.

Molds for Hyperier also have to be modified to make a good weld. “They need a dam and bead placed in the flash pockets parallel to the pinch-off to force the melted material into the mold cavity as the mold is being closed,” Mergon’s Thompson notes. Otherwise there can be gaps in the weld seam. Mergon reports trials with eight different formulations, including black material and black material with regrind, which all met permeation levels of <1.5 g/sq m per day. Mergon has used Hyperier commercially in up to six-gallon tanks with up to 30% regrind. LG makes Hyperier in three grades for small (1-10 liter), medium (5-20 liter) and large (20-220 liter) containers. Grades for larger parts have lower specific gravity and higher impact strength, but the distinction doesn’t seem critical because LG’s website shows a 5-gallon portable fuel can and a 2-liter gas tank both made with Hyperier IP1105.

In November 2009, Mergon started trials with Enbarr 2020BN, made by Nano Polymer Composites in Taiwan (www.nanopolymer.com), and distributed in the U.S. by Enbarr LLC in Merritt Island, Fla. (www.enbarr.com). Enbarr 2020 is a nanocomposite made of nylon 6.6 and volcanic ash, or pumice, developed originally for the heat shield on the space shuttle. Enbarr isn’t a blending material, but is used at 100% and can get extremely low permeation levels of <0.1g/m2/day with a 5 mm thick wall. Enbarr has a more forgiving temperature profile than Hyperier, but is hard to deflash. Mergon needed a larger blow molding machine to have enough clamp force to get flash off. Nano Polymer is making a new formulation for better deflashing, which Mergon hopes to test early next year. Historically Enbarr 2020 cost $4-$5/lb, which is too expensive for most gas tanks. Being nylon it also has a problem with cold temperature drop tests.

Mergon, which has up to three-layer coex capability, also tested new barrier materials for coextrusion.  In 2007 Mergon began testing Ixef BXT, then a developmental blow molding grade of polyarylamide (PARA) from Solvay Advanced Polymers LLC in Alpharetta, Ga. (www.solvay.com). Solvay received CARB approval for Ixef in gas tanks in 2008, presented it at blow molding conferences in 2009 and 2010, and commercialized it this year. It can be used as a barrier layer with HDPE either with tie layers or by blending adhesive into the HDPE. Solvay has tested it in a three-layer sandwich and in two layers with Ixef as the inner layer. Mergon plans three-layer trials with it next year.

Six months ago Mergon began testing TIEVOH, a custom compound made by Enbarr,  combining EVOH and tie layer adhesive. TIEVOH bonds directly to HDPE without a tie layer, so a three-layer coex machine can make EVOH barrier tanks. Enbarr recommends 3-5% TIEVOH because tanks with over 2% EVOH overall can be certified by design by the EPA. They would still, however, require soak, durability and permeation testing in California. Mergon is developing three-layer TIEVOH marine gas tanks for a sister company of Enbarr, BluSkies International LLC in St. Charles, Ill. (www.bluskies.us). TIEVOH is already commercial in a rotomolding formulation for large three-layer installed marine gas tanks.

In 2012 Mergon has scheduled trials with Hostaform LP CKX5622, a grade of POM (polyoxymethylene) from Ticona Engineering Polymers, Florence, Ky. (www.ticona.com) also for coextrusion. Hostaform POM is an acetal copolymer (originally Celcon from Celanese), which needs to be dried. Mergon has also scheduled tests with Nylene 764B, a barrier material from Gulf View Plastics Inc., Hudson, Fla. (www.gulfviewplastics.com), which is approved in California. “We may never go into production with a lot of these materials,” Mergon’s Thompson says, “but we will have proven out the materials, and we’ll know how to use them.”

Mold designs for monolayer barrier gas tanks made with Hyperier/HDPE blends have to be modified at the pinch off to force more melt into the mold cavity. Otherwise there can be gaps in the weld line.

NEW FLEXIBILITY FOR SIX LAYER BARRIER

Six-layer EVOH barrier is also expanding for high-barrier blow molded gas tanks. Agri-Industrial Plastics Co., Fairfield, Ia., an exhibitor at the blow molding conference (www.agriindustrialplastics.com), announced a major investment in new six-layer barrier capacity. Agri currently operates three six-layer blow molding machines from Kautex Maschinenbau GmbH in Germany (www.kautex-group.com), making barrier gas tanks for a variety of non-automotive applications in the 3-50 gallon size range. It’s buying two new six-layer continuous coextrusion blow molding machines—a KBS241 with 900 kg/hr throughput and a KBS61 Smart with 750 kg/hr throughput, both for delivery next summer. The new machines will have six-axis robots and quick head and mold change capability “for more flexibility in shorter runs of gas tanks for all-terrain vehicles, snow mobiles, personal watercraft, golf carts, and lawn equipment,” says Agri sales manager Mick Stielow.

Blow molder Agri-Industrial is expanding its six-layer coex blow molding capacity from three machines to five to make high-barrier gas tanks for off-road engines. Kautex is building the new machines with six-axis robots and fast tool change for flexibility for shorter production runs.

Compliance whether with new CARB or old EPA levels is essential.  The EPA can, afterall, take any lawnmower or power boat out of a dealer’s showroom, and if the gas tanks aren’t certified, or the information on the certification turns out to be false, the penalties can be stiff—up to a maximum of $37,500 per gas tank model!

*Update 1/23/2012: In the initial publishing of this blog, we referenced a 2002 report from CARB that showed two tanks from Fluoro-Seal International LP not reaching the permeation levels currently required in the 2012 update from CARB.  We have since learned that an addendum to that report cites carbon black bias in the initial results.  We regret the error.

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Neat New Stuff from the First Eurotec

The SPE’s first Eurotec conference, November 14-15 in Barcelona, Spain, is a European version of ANTEC, the SPE’s perennial conference highlighting new technology. Publications for the inaugural Eurotec didn’t have to be absolutely new the way ANTEC papers do. Still the conference assembled an impressive array of technologies presented either for the first time, or for the first time to a general plastics audience.

Two papers presented new multi-step combinations of different processing technologies, involving some kind of self-closing mold. Two papers described new compounds with properties enhanced by specially synthesized round polymer particles or molecules. Two papers described processes that replace all or part of the friction heat of plasticizing with convection heat for lower shear. Several papers described new starch based biopolymers, including a microwave-foamed starch and barley fiber composite plastic.

NEW INJECTION MOLDING TECHNOLOGIES

“Stages Molding: A Novel Technology to Produce Plastic Parts” by Miguel Rodriguez-Perez, director of the Cellular Materials Lab of the University of Valladolid in Spain (www.cellmat.es). The patent-pending technology uses self-closing molds, which require no outside clamp pressure, and allows very low pressure molding (typically below 15 bar). Molds are filled with pellets or molten plastic, then the mold itself is heated either with hot oil or electric resistance heaters. Pressure can be created by a chemical blowing agent in the material for foam-core parts or by a hydraulic manifold for solid parts. The process is being used commercially and can make large parts with reduced weight. ABN Pipe Systems Group in A Coruna, Spain, is a research partner in the development.

“New Processes for Large Scale Automotive Production of Composite Applications” by Marcus Schuck, director of R&D, Jacob Plastics GmbH, Wilhelmsdorf, Germany (www.jacobplastics.com). This new technology, developed over the past three years and now in prototype, combines injection and compression molding to create complex hollow parts in a single tool. FIT Hybrid (fluid injection technology), which won a Germany technology award in 2010 and a JEC innovation award in France earlier this year, makes a tube-like hollow thermoplastic composite. First two thermoplastic textile sheets are preheated with IR radiation; plastic is then injected between the sheets to make a sandwich preform. An injection mold closes over the preform, pinching and embossing the edges. Gas is then injected into the mold to shape a hollow part, driving most of the “filling” plastic out of the mold. The hollow part can then be over-molded with ribs and other solid features.

Jacob Plastic’s FIT (fluid injection technology) preheats two sheets of polymeric fabric, injects plastic between them like a sandwich, then closes and embosses the sandwich in a two-sided tool. Gas is injected forcing the “filling” polymer out to form a hollow part, which can then be over-molded.

“Impress, an Innovative Pilot Injection-Compression Molding Platform for the Production of Micro-Nanostructures on Plastic Parts” by Mael Moguedet, head of plastronics business, PEP Centre Technique de la Plasturgie, Oyonnax, France (www.poleplasturgie.net). IMPRESS adds micro-nano (100-500 nm ) surface features to molded plastic using “self assembly” coatings, interference lithography, nano lasers, and plasma etching. Micro nano patterned nickel shims are being tested in molds at partner plants now.

A consortium including PEP in France and CSEM in Switzerland is developing Impress mold inserts like these nickel shims to emboss micro-nano (100-500 nm) features. Shown are sample impressions in polycarbonate. PHOTOS: CSEM

NEW EXTRUSION AND FILM TECHNOLOGIES

Natural Gas as Main Energy Source for Polymer Plasticizing with a Specially Designed Heat Exchanger by Felix Heinzler, research assistant, Institute of Engineering and Plastics Machinery,  University of Duisburg-Essen in Germany (www.uni-due.de).  A lab-scale demonstration device melts plastic in a gas-fired barrel heater with a specially designed heat exchanger and a melt-pump to move the plastic. Plasticising polymers without friction saves energy cost and allows almost shear-free extrusion.

The University of Duisburg’s new primary-energy-based plasticizing unit has a short screw only to convey and preheat pellets. Melting is done by a gas-fired barrel-heater with a heat exchanger, allowing almost shear-free extrusion.

“New and Improved Screw Technology for Processing NatureWorks INGEO” by Timothy Womer, president of TWWomer & Associates LLC, Edinburg, Pa. (www.twwomer.com). A modified barrier screw design for PLA produces melted and semi-melted material pools, which are homogenized and fully melted using convection heat in a special distributive mixer. The PLA screw is being tested by NatureWorks LLC, Minntonka, Minn. (www.natureworksllc.com), and is available from machine builder R&B Plastics Machinery, Saline, Mich. (www.rbplasticsmachinery.com).

“Production of a Functional 3D Plastic Pane” by Ralf-Urs Giesen, researcher, University of Kassel in Germany (www.uni-kassel.de). A 7-layer polycarbonate panel is being developed for car sun roofs, which will be able to change from clear to blue to keep the car interior cool. First is a clear PC substrate, then a conducting indium-tin-oxide layer is sputtered on, then an electrochromic layer of PEDT/PSS (poly 3,4 ethylenedioxythiophene/polystyrene sulfonate), followed by a thick layer of an ion conducting polymer electrolyte, then an ion storage layer of TIO2, another conductive indium-tin-oxide layer, and finally another structural layer of PC. The university is now checking the thermoformability of the layers. Sunroofs could also be injection molded behind a functional film with the same layers.

Researchers at the University of Kassel are adding colloids, spherical particles of cross-linked polymer chains, at up to 15 wt% to polymers of the same monomer to improve flex modulus and impact properties without hurting clarity. Illustration shows a PMMA polymer matrix.

“Strain Hardening: An Elegant and Fast Method to Predict the Slow Crack Growth Behavior of HDPE Pipe Materials” by Linda Havermans, lead scientist, SABIC Technology and Innovation, Geleen, the Netherlands (www.sabic-europe.com). A clever short-cut can test PE pipe resins for slow crack growth. The ASTM standard test, known as the Notched Pipe Test, or NPT, can take up to a year of testing and requires a lot of pipe. The full notch creep test (FNCT) requires only a few 100 grams of plastic, but takes just as long. SABIC found that testing strain hardening modulus, from a stress-strain curve at 80 degrees C, correlates perfectly with the results of both the NPT and FNCT, and can be done in a lab in only a few hours using little material. SABIC uses this method for material development and quality control and suggests the test as an easy, inexpensive way for pipe converters to test incoming resin lots for crack resistance.

NEW COMPOUNDING TECHNOLOGIES

 “Modification of Amorphous Plastics by Compounding with Colloids” by Viola Sauer, scientific assistant, Institute for Materials Engineering – Polymer Technology, University of Kassel in Germany (www.uni-kassel.de). Colloids are spherical knot-like particles of cross-linked polymer chains, which can be penetrated by other polymer chains of the same monomer when mixed in a suitable solvent. Synthetically creating colloids and conventionally compounding them into a similar polymer—in this case PMMA colloids into PMMA–improves flex modulus and impact strength without hurting clarity. Colloidal composites were tested with up to 15% dry colloid content.

“High Flow Glass-Fiber-Filled Aromatic Polyamide Resins” by Frans Mercx, chief scientist, LNP technology team leader, SABIC Technology and Innovation, Bergen op Zoom, the Netherlands (www.sabic-ip.com). SABIC has investigated highly branched dendritic aliphatic polyester molecules as flow enhancers, using dendritic molecules with 32 terminal OH groups and mol. wt of 3600, more than twice the normal size. At 0.5 to 1% loading in highly glass-filled nylons (30%, 40% and even 50%) melt flow rate improves over 100% without hurting mechanical properties.

NEW BIOPOLYMER MATERIALS

“2,5-furandicarboxylic Acid (FDCA); A Versatile Building Block for a Very Interesting Class of Polyesters” by Matheus Dam, team leader at Avantium Chemicals BV, Amsterdam, the Netherlands (www.avantium.com).  Shell spin-off Avantium is bringing a 40-ton-yr pilot plant on-stream in Holland to make FDCA (2,5-furandicarboxylic acid),  a new monomer to make PEF (polyethylene furanate). PEF will be a new bio-based polyester that is like PET, but has six-times better barrier properties targeting all-biopolymer beverage bottles.

“Silicone Modified Bio-based Coatings from Soyabean Oil for Water Resistant Papers” by Shilpa Manjure, manager of product development, Northern Technologies International Corp., Circle Pines, Minn. (www.ntic.com). This developmental biopolymer coating is made of soybean oil bonded to vinyl trimethoxy silane in the presence of peroxide. The patent-applied-for technology (U.S. Pat. Applic. # 2010008387), licensed from Michigan State Univ. (www.msu.edu), targets waterproof coatings on paper for food packaging and was funded by the Department of Defense. If the silanol cured at ambient moisture, it is low in viscosity and would soak into paper. So the silanol is partially cured with heat and 4% water to make it thick enough for coating.

“FlourPlast: Creating New Opportunities for the Bioplastic Industry. Process Structure Property Relationships of a Novel Bioplastic Polymer” by Jeroen van Soest, innovation manager, Rodenburg Biopolymers and Optimum Bio Plastics, Oosterhout, the Netherlands (www.biopolymers.nl). Optimum offers a family of pelletized thermoplastic flours made by melt-compounding the starch, proteins, sugars, fats and fibers in the flour with vinyl acetate copolymer. Pelletized FlourPlast grades range from flexible to rigid for melt blending into biopolymers like PLA or PHA or polyolefins like PE or PP. They have been commercial for about a year and are available in the U.S.

“Development of Starch-Biobased and Biodegradable Plastics for Use in Trays for Food-Packaging” by Alberto Lopez-Gil, biopolymer researcher at the Cellular Materials Lab of the University of Valladolid in Spain (www.cellmat.es). A novel replacement for foamed PS trays is being developed out of starch-based polymer reinforced with barley straw fiber. It can be foamed using microwave heat, which is absorbed by moisture in the starch polymer composite, resulting in a light-weight bio-based plastic.

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GPEC Debuts Two New Closed-Loop Recycling Processes and a New Algae Plastic

At the SPE’s Global Plastics Environmental Conference (www.sperecycling.org) in Atlanta in October, two new recycling operations were introduced along with a brand new algae bioplastic. The new recycling processes are sophisticated closed-loops for complex post-consumer materials—shredded plastic from household appliances in Japan and PVC roofing in North America–both driven initially by legislation. The new bioplastic is possibly the first directly plasticized from algae. Non-attendees can buy the papers from GPEC 2011 on CD ROM for $75.00 (email: ssola@mrcpolymers.com).

NEW PROCESS RECYCLES MIXED APPLIANCE PLASTIC IN JAPAN

Mitsubishi Electric Corp. in Japan (www.mitsubishielectric.com) took over 10 years to develop technologies in house to recycle plastic from shredded air-conditioners, TVs, refrigerators and washing machines into 99% pure PP, PS and ABS, all used in new Mitsubishi air conditioners. Mitsubishi’s website posts English language reports on the technology, but GPEC was its first presentation outside of Japan.

The first stage of the technology is wet separation of mixed plastic flakes into three densities: unfilled PP with under 1.0 specific gravity separated by float/sink; a mixture of PS and ABS with 1.0 to 1.1 specific gravity separated by oscillating water flow; and everything heavier than 1.1 specific gravity (PC/ABS alloys, PVC and highly filled plastics) burned for energy recovery. PS and ABS are then separated from each other electrostaticly.

Mitsubishi also developed a patent-applied-for X-ray transmission separation technology (WO 2010/092645 and JP2009198387) to remove bromine-containing flake from the PP, PS and ABS, which otherwise wouldn’t comply with the European Union’s RoHS Directive. The directive restricts the presence of bromine, chiefly polybrominated diphenyl ether flame retardant, to below 1000 PPM in new electrical appliances and electronics. “We developed a line-scanning and rapid screening system using the X-ray transmittance difference of bromine content. This system can screen and separate plastic flakes 100 times faster than the florescent X-ray method,” reports Koji Hamano, manager of eco materials at Mitsubishi Electric’s advanced technology R&D center. The separated flakes pass on a conveyor at 100 m/min. between an X-ray transmitter over the conveyor and an X-ray line sensor under it. Brominated flakes transmit less radiation than unbrominated flakes and appear darker. A data processor instructs an array of 124 individually controlled air jets to remove brominated flakes. The technology won the 2010 Environmental Award from Japan’s Ministry of the Environment.

Green Cycle Systems Corp (a unit of Mitsubishi) in Chiba, Japan, opened in April, 2010, using the new process to recycle 22 million lb/yr of incoming shredded appliance plastic, yielding 14 million lb/yr of purified plastic. Green Cycle gets all feedstock from another Mitsubishi subsidiary, Hyper Cycle Systems Corp., set up in 1999 to comply with Japan’s Home Appliance Recycling Law. Hyper Cycle crushes used appliances, removes metals and other impurities, shreds the plastic into 10 mm flakes, and removes fines. The mix is 30% PP, 40% ABS and PS combined, and 30% heavier plastics.

Only a few other companies in the world tackle mixed post-consumer durable plastics, which often include WEEE (waste electrical and electronic equipment) and ASR (auto shredder residue) and are more complex. MBA Polymers in Richmond, Calif., has about 300 million lb/yr of processing capacity for mixed WEEE plastics and ASR, producing ABS, HIPS, PP, HDPE, rubber, and mixed plastics for lower-end applications. MBA assembled a proprietary series of recycling technologies, but didn’t invent the components. Mitsubishi could have bought available components too, but wanted high volumes and started from scratch.

Mitsubishi Electric recycles shredded appliance plastic with float/sink, oscillating water and electrostatic separation. It developed its own X-ray transmission technology to identify brominated flake, which are removed by 124 individually controlled air jets.

 

 

 

FIRST N. AMERICAN RECYCLING OF POST-CONSUMER PVC ROOFING

The Sarnafil Services division of Sika Corp. in Canton, Mass. (www.sarnafil.sika.com), a maker of industrial vinyl roofing, is believed to be the first in North America to recycle post-consumer vinyl roofing back into new PVC roofing. Sarnafil collects used roofing in 40,000 lb truckloads from contractors installing new Sarnafil roofs. The concept only works with large roof areas, but 80% of Sarnafil’s business is replacement of industrial roofs. Contractors cut old roofing into 3 ft wide sections, roll them tightly, and pack them in reusable Gaylord containers provided by Sarnafil and collected for free, initially to support customers in areas with landfill restrictions on construction waste.

European roofing manufacturers operate a similar closed loop recycling program for members, called Roofcollect (www.roofcollect.com), of which Sarnafil’s Swiss parent Sika is a member. Roofcollect has been active for over 10 years and reports collecting over 3 million lb of post-consumer PVC roofing in 2010. Sarnafil, which started its program in 2005, will recover close to 600,000 lb of post-consumer PVC roofing this year, using the material as a mineral filler at up to 4.5% in the back ply for new vinyl roofing. Several of Sarnafil’s customers have won awards for participating, but GPEC was the first presentation of the program itself.

Sarnafil’s post-consumer roofing is recycled on a toll basis by Norwich Plastics in Cambridge, Ont. (www.norwichplastics.com), which has specialized in post-consumer PVC recycling, primarily from wire and cable, since the 1980s. Norwich almost turned down the job at first because of the cross-linking challenge. Post-consumer PVC roofing is all different durometers based on age. Roofs are exposed to extreme UV radiation, so over time thermoplastic PVC cross-links and doesn’t melt any more. Sometimes roofs are replaced that are under 10 years old and still have good melt properties; sometimes roofs are so old and brittle that they are just mineral filler and backing; and they can be anywhere in between.

Norwich tests each incoming lot for durometer, washes the roofing, then grinds and elutriates it to remove fluff from old polyester backing. Initial testing, grinding and elutriation are done at any of several Norwich plants, based on proximity. Ground and elutriated material then goes to Norwich’s Woodstock, Ont., plant to be cryogenically ground a second time into 20-mesh powder and blended for uniform properties. Norwich has also begun compounding and pelletizing post-consumer powder with pre-consumer PVC into masterbatch with about 30/70 post-consumer and pre-consumer PVC. Sarnafil says this should enable them to increase recycled content in new roofing.

Sarnafil collects post-consumer PVC roofing from customers, testing each lot for durometer, which varies from thermoplastic to fully cross-linked depending on age. A toll recycler converts it into fine powder and 30% recycled pellets for new roofing.

 

 

 

NEW SOURCE OF ALGAE PLASTIC

Algix LLC in Bogart, Ga. (www.algixllc.com), is blending high-protein-content algae with thermoplastics to make new bioplastics for disposable and durable applications. A spin-off from the University of Georgia in Athens, Algix co-owns patents on algae technology (relating mostly to biofuels) with the university and licenses the concept of direct plasticization of algae from Kimberly-Clark Corp., Dallas, Texas (www.kimberly-clark.com). Kimberly-Clark’s patent-applied-for technology (U.S. Pat. Applic. # 20100272940) focuses on blends of thermoplastic algae and polymers like PE or polyesters.

Algix and Kimberly-Clark aren’t the only companies to blend algae directly with thermoplastics. Cereplast in Hawthorne, Calif. (www.cereplast.com) in early 2009 announced plans to commercialize up to 50/50 blends of algae and PP when sufficient supplies of algae biomass became available. Cereplast sources dried algae as residue after extraction of oils from the algae. Kimberly-Clark’s patent also refers to future algae fuel production as a possible source.

Algix, however, is working on a different source. Ryan Hunt, director of R&D at Algix, wants dairy farmers to raise algae as a new cash crop, while remediating water runoff. Instead of causing algae blooms in local ponds and streams, farmers can use a commercial remediation system called an Algal Turf Scrubber, available from HydroMentia Inc., Ocala, Fla. (www.hydromentia.com). It has a large 3.5 acre PE mat graded at a slight 2-degree angle, over which polluted water flows constantly. In about a month a thick mat of algae grows, which can be removed by a tractor pulling a scraper. Mats of algae are currently composted, landfilled, or fed to cattle. Algix wants to make them into bioplastics.

Algix works with Ven Consulting LLC in Melbourne, Fla. (www.venconsultingllc.com) to harvest, dry and mill algae biomass for conversion into plastics. The best protein sources, Algix says, are two micro algae, Chlorella vulgaris and Spirulina Platensis, and filamentous algae  and macrophytes from the Lemna and Cladophora genuses. Chlorella is 55 dry wt % protein, 15% starch, and 18% fat with low ash and fiber. Spirulina is 55% protein, 11% starch, and 5% fat, also with low ash and fiber. Cladophora can have up to 40% protein, 20% fiber and 30% ash. Kimberly-Clark’s patent also describes plasticizing a third micro algae, Nanochloropsis, a popular strain for algal oil production. All are less than 115 microns in size. Research at the University of Georgia has also shown that nano-cellulosic fibers from Duckweed have similar performance to aramid fibers (Kevlar).

Pure algae plastic made by compression molding is hard like PS, but brittle. Algix blends powdered algae with powdered HMW HDPE (53-75 micron) with a melt temperature of 144 degrees C, and glycerol as a plasticizer for flexibility. Algae biomass burns at 200 degrees C, which limits formulations to polymers with melt temperatures below 190 degrees C. Algix presented data on compression molded blends of 30/50/20 HDPE/algae/glycerol, but has tested over 30 formulations for extrusion compounding and injection molding, including blends of algae and macrophytes with PLA to make 100% bioplastics. Compounding was done on a 21-mm-diameter Theysson twin-screw extruder in the Polymers Center of Excellence (www.polymers-center.org) in Charlotte, N.C.

Algix’s algae plastics are black or dark brown, unless made into thin film, which can be blue green. Cereplast’s compression molded algae plastic from biomass after oil extraction is olive green. Algix still needs to overcome problems with color and odor. Kimberly-Clark’s patent describes bleaching algae to produce off-white or light yellow plastic. Cereplast reports that it has solved the odor problem. Chlorella smells earthy, Spirulina smells like fish food, and macrophytes smell like fresh cut grass when processed. Algix’s target price for finished algal bioplastics is $1/lb. It is looking for strategic partners for scale up and distribution.

University of Georgia spin off Algix is developing new bioplastics made directly from algae. Algae are dried, milled, and extrusion compounded with polymers like PE or PLA to improve brittleness. Kimberly-Clark owns the concept.

 

 

 

 

 

 

 

 

 

Several student posters presented at GPEC 2011 reflect the same themes, notably “Algae biocomposites produced from biomass co-product” by Alejandra Constante from the University of Alabama at Birmingham; “Duckweed Aquatic Macrophyte with the Potential for Sustainable Materials Production” by Renuka Dhandapani from the University of Georgia, Athens (the same group that spawned Algix); “Morphology and properties of thermoplastic sugar beet and PLA” by Peng Zhan from Washington State University, Pullman; and “Bio-renewable Carbon fiber precursor from lignin” by Keke Chen from Iowa State University, Ames. Information on student posters can be downloaded from www.sperecycling.org.

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And the Biggest Loser Is…

One of the most competitive areas in automotive technologies these days is weight loss. American carmakers need to lighten cars to improve fuel efficiency and offset weight added by more advanced gadgets. European carmakers are under even more pressure to lose weight because they have to reduce CO2 emissions (to 130 g/km) for 65% of new cars starting next year and for all cars by 2015. So chemists, compounders, and engineers are finding creative new ways to replace heavy materials with light.

Here are some of the latest developments in automotive lightweighting, introduced at two current conferences from the Society of Plastics Engineers’ Automotive and Composites Division and Detroit Section in Troy, Mich.–the Automotive Composites Conference & Exhibition Sept. 13-15 (speautomotive.com/comp), and the 2011 Automotive TPO Conference Oct. 3-5 (auto-tpo.com), both held in Troy.

The ACCE conference introduced a new super lightweight continuous-glass thermoplastic molding technology for the first time. The TPO conference features several new technologies to reduce weight by reducing talc, including the first beta nucleation of talc-filled PP and the first part validation of a new magnesium-based fiber. The percentage of weight saving is less dramatic than from glass reduction, but still significant. The ACCE papers will be available free at http://speautomotive.com/aca at the end of the year.

REDUCING WEIGHT BY REDUCING GLASS

At the ACCE conference, a paper from Timo Huber, an engineer at the Fraunhofer Institut in Pfinztal, Germany (www.ict.fraunhofer.de), presented “Local Continuous Fiber Reinforcement” technology for the first time anywhere. (The paper was published in the proceedings for a conference in Marakesh earlier this year, but wasn’t actually given.) The technology places heated continuous glass fiber around metal inserts, only where needed along stress axes in the part and can save up to 80 wt% of glass vs glass-filled PP.

The Fraunhofer Institut’s new continuous glass-fiber molding puts hot glass roving around metal inserts along stress axes in a part, reducing glass content by up to 80%.

Continuous-fiber-reinforced structures have been molded before using woven fiber glass shapes and unidirectional fiberglass tape, like the auto seat system developed by BASF Corp. (www.basf.com) and the French auto parts maker Faurecia (www.faurecia.com), which was originally introduced as a concept at auto shows three years ago. (It was also presented at the ACCE.) Both BASF/Faurecia and Fraunhofer’s continuous glass thermoplastic parts create a separate glass-reinforced structure, place it in the mold, and mold over it. Both achieve dramatic weight savings replacing metal. But Fraunhofer’s cats-cradle approach to glass roving is about as minimal and strategic as glass use gets.

Fraunhofer starts by making unidirectional roving out of commingled PP and glass fiber, first heated, then pulled over three consolidating rollers for even distribution and wetting, and then pulled through a die for shaping. Temperatures in the heating zone, consolidating rollers and die are important to make roving without voids, Huber says. The roving is hand placed over the pins while hot, but in production could be placed by robot. Non-metal pins could also be used, and automotive parts that already have metal thread inserts for attachment points can use these to hold the glass fiber roving. Roving can be designed into structural ribs for further weight saving.

Sample parts with 6.5 wt% unidirectional glass showed higher tensile strength than glass-filled composites with 30% of either long or short glass fiber. Samples with only 2.3 wt% unidirectional glass achieved nearly the same tensile strength as 15% short or long glass composites—approximately 47 MPa for continuous glass vs. 49 MPa for short glass and 52 MPa for long glass. All parts were molded with impact copolymer PP (C711-70RNA from Dow Chemical), which has a MFR of 70 g/10 min.

Two papers present successful cross-linking of PP, which is unusual in itself. At the ACCE conference, Scott Miller, application engineer at Dow Corning Corp., Midland, Mich. (www.dowcorning.com), reported on “Closing the Gap Between PP and PA Composites with New Silane Grafting Technology” (initially presented at the SPE’s ANTEC conference in May). Dow Corning calls it the first successful free-radical silane grafting of PP while minimizing beta scission. Chemical grafting and cross-linking of PP typically break molecular chains and reduce properties. PP can be commercially grafted with chain extenders like maleic anhydride, but these only allow coupling to fibers, not cross-linking.

The patent-applied-for technology (U.S. Pat. Applic. # 20110178198) grafts a silane molecule onto the backbone of the PP chain. Silane-grafted PP can then either couple either with reinforcing fibers, cross-link neat PP, or do both to improve performance. Dow Corning’s silane-grafting technology shows improvements over maleated PP for heat stability, long-term aging, moisture resistance and mechanical strength with fibers, Dow Corning says. It has been successfully tested with glass, flax, hemp, ligno cellulosic, and wood fibers and reportedly improves bio-fiber composites enough to replace glass in some applications.

In the TPO conference, Jesse Baldwin, technical director of Toray Plastics (America) Inc.’s foam division in Front Royal, Va., (www.torayfoam.com), will present “New Cross-Linked Olefin Foams for Soft Touch Automotive Interior Trim Applications.” The patent-applied-for (U.S. Pat. Applic. # 20110014835) ToraSoft foam is a closed-cell PP foam with a combination of extreme softness–70% softer than Toray’s previous PP foams–with good haptics, or sense of touch and feel, good thermoformability, and good rebound characteristics. According to the patent application, it combines an olefin block copolymer with PP, a chemical blowing agent, and chemical cross-linking agent. The extruded sheet is cross-linked with an electron beam and heated for foaming in a molten bed of salt, a process Toray has used since the 1960s for even heat transfer and free foam expansion. ToraSoft, introduced commercially in January 2010, is under qualification and has been specified for upcoming automotive programs for interior trim parts.

WEIGHT-WATCHER RECIPES FOR TPO

Several recent developments introduced at the TPO conference take weight out of TPO parts by reducing EPDM rubber or talc. Philip Jacoby, v.p. of technology at Mayzo Corp., a specialty chemical company in Suwanee, Ga., (www.mayzo.com) will present “New PP Beta Nucleation Technology for Improving the Impact-Stiffness Balance of Neat and Talc-Filled PP and TPO Parts.” Beta nucleation is unusual in the first place. (A few Asian companies also make beta nucleants, but Mayzo believes it is the only maker of beta nucleant masterbatches.) Mayzo’s new third-generation beta nucleant masterbatch, MPM 2000, however, has the highest beta nucleating activity anywhere. It can reportedly produce PP with up to 70% of crystals in beta form. The crystal phase of homopolymer PP is typically over 95% alpha crystalline, which melts at 165 degrees C, and only 5% beta crystals, which melt at 14-15 degrees C lower temperature.

Mayzo’s new high-activity beta nucleant masterbatch can make PP with 70% hexagonal beta-form crystals for greater strength and lighter weight. During thermoforming beta crystals convert to alpha crystals, leave micro voids, and turn the plastic white.

Beta nucleation produces hexagonal crystals in PP, whereas alpha nucleation produces clusters of monoclinic crystals (a rectangular prism with a parallelogram at its base). Hexagonal beta crystals improve impact strength and impart opacity, but lower tensile strength and flex modulus. By improving impact strength of talc-filled TPOs, beta nucleation allows APDM reduction. Mayzo introduced beta nucleant masterbatches commercially six years ago, but the first two versions had the limitation that they couldn’t be used with alpha nucleants like talc, certain pigments, or alpha-nucleated PP, which many resin producers make by adding sodium benzoate, NA-11, NA-21 or the clarifier Millad 3988. Mayzo’s second-generation beta nucleant solved the problem by adding an alpha nucleator “killer,” which prevented interference from sodium benzoate, but did not stop other alpha nucleants.

The new third-generation beta nucleant overcomes alpha nucleation by very high activity of the beta nucleator. Beta-nucleated PP can also make breathable biaxially oriented, waterproof film with densities as low as 0.28 g/cc. During biaxial stretching or thermoforming, beta crystals convert to alpha crystals and form micro voids, making the plastic white without pigment. When thermoforming web scrap is reprocessed, however, the beta nucleant is still present and retains its initial nucleation activity, so new beta nucleant only has to be added for the 50% that is virgin material.

At the TPO conference Wouter Reyntjens, business development manager at Milliken & Company, headquartered in Spartanburg, S.C. (www.millikenchemical.com) is presenting an ongoing OEM validation of a recently introduced magnesium-based synthetic mineral fiber reinforcement. The fiber, called Hyperform HPR803i, was introduced two years ago at the 2009 National Plastics Exposition in Chicago, but this is the first data on a part. HPR803i is 99% magnesium oxysulfate according to the MSDS with high aspect ratio and is sold in powder form. Loaded at 3%-10% with or without talc, it reportedly achieves better scratch resistance than PP with talc alone and weight savings from reduced talc of 7%-20%, depending on part requirements.

Milliken will present data on a developmental B-pillar trim part, made by Mecaplast Group, a tier-one automotive molder in Monaco (www.mecaplast.com), using a compound developed by Inno-Comp Ltd., a compounder in Hungary (www.inno-comp.hu). The compound has 13% mineral loading of talc and HPR-803i with a density of 0.98 g/cc and performs like 20% talc-filled PP for a density of 1.04 g/cc. But it weighs 7% less and has better scratch resistance.

This B-pillar trim part made with Milliken’s recently introduced HPR803i magnesium-based fiber and reduced talc weighs 7% less than 20% talc-filled PP and has better scratch resistance.

 

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Developmental Extrusion Process ‘Spins’ Powder

When you grind plastic cryogenically into powder, it has microscopic sharp edges and angles, which lower bulk density and processability. Cryogenic grinding is also expensive and energy consuming. Theoretically if you could extrude micropellets five or ten times smaller than conventional micropellets, you would have round powder with higher bulk density and better processability. That’s what Tim Osswald, a professor at the polymer engineering center at the University of Wisconsin-Madison, thought when he got an idea for extruding powder.

Simulation (in red) and microphotography show how corrugations or waves, known as Rayleigh disturbances, form in a thread of polymer and break off into micro droplets. Source: Univ. of Wisconsin-Madison

The idea came from the way two polymers are compounded: one polymer forms round domains or droplets in a matrix of the other polymer. Osswald thought if he could extrude a thin thread of plastic and stretch it thinner with hot moving air, the air would act like the matrix and break the polymer thread into small round domains. The phenomenon is called Rayleigh disturbances from Lord Rayleigh, a British physicist, who developed a model for water drop formation in the late 1800s.

“The idea was that with several nozzles, you could produce high-volume micropellets or powders like fiber spinning,” Osswald explains. Powders are used for rotational molding, microinjection molding, compression molding, sintering of microporous parts and selective laser sintering (SLS) processes for rapid prototyping. In injection molding higher bulk density allows faster cycle times and filling of very narrow molds. In compression molding it fills molds more efficiently with lower press height. Powders also have potential for sintering mold-less production parts.

In the Univ. of Wisconsin’s developmental extrusion process for powders, different polymers make powder with shapes. HDPE forms smooth, lemon-shaped micropellet powder, while LDPE forms larger, rougher, bean-shaped micropellet powder.

When Osswald described his idea for a nozzle that could spray micropellet powders to colleagues, they thought it was interesting, but wouldn’t work. When he applied to the National Science Foundation in 2009 for a grant to build a prototype, four reviewers also praised the concept as interesting, but thought it wouldn’t work and turned it down.

Osswald then used a grant that accompanies his K.K. and Cindy Wang professorship (K.K. Wang is the founder of C-Mold, a developer of CAE software that is now part of Autodesk) to build the prototype. It worked from the get go. “We made little tiny droplets between 20 and 500 microns,” Osswald recalls. “Depending on how you adjust it, you can get the micro droplets all the same size.” By comparison, conventional underwater micropelletizing dies produce micropellets down to about 500 microns in size.

The patent-applied-for technology was presented for the first time in two papers given at ANTEC in Boston last May by Osswald and Martin Launhardt, a graduate student who built the prototype: “Manufacturing of Micropellets Using Rayleigh Disturbances” and by William Aquite, a graduate student who simulated the process: “Simulation of Micropelletizing Mechanisms.” A CD of all ANTEC papers is available to non-attendees for $150 from the SPE (www.4spe.org).

Grinding isn’t the only way to make powder. Polyolefin reactors produce powders, mostly irregular in shape with low bulk density,so they are pelletized. But some HDPE powders are used directly from the reactor. Size depends on catalyst type. Chromium-based catalysts make coarse 800-micron HDPE powder, which is used a lot in wood-plastic-composite lumber and masterbatches. Ziegler-Natta catalysts make finer 150-micron HDPE powder, including bimodal powders used to impart crack resistance in pipe.

Powders are also made in secondary solution and precipitation processes. The Equistar division of LyondellBasell (www.lyondellbasell.com) has made 20-micron round Microthene powders for 30 years out of EVA, HDPE, LDPE and PP in a proprietary solution process using high-speed sheer stirring (the original patent from 1973, U.S. Pat. # 3746681, has expired). But these are specialty powders used as additives in inks, coatings, lubricants, and cosmetics, not for melt processing. (An excellent description of powder markets is found in an ANTEC paper from 2005 called “Higher Performance Polyethylene Powders” by James Krohn, Brandon Hughes, and others from Equistar.) Precipitation processes are also used commercially to make powder, but don’t work with every polymer, such as POM (polyoxymethylene) and PLA (polylactic acid).

HOW POWDER EXTRUSION WORKS

The micropelletizing setup at the University of Wisconsin starts with a ¾-in. Brabender lab extruder. Melt flows from there through a half-inch-diameter melt tube in the feed block, makes a right angle turn and flows downward into a capillary tube 1 mm diameter and 22.5 mm long. This forces the melt to stretch and speed up.

When melt exits the capillary die, it’s pulled downward and stretched again “by a stream of hot air coming out of a coaxial annular orifice with an external diameter of 3 mm and inner diameter of 1 mm,” Osswald’s paper explains. (The inner diameter is the outside of the capillary tube.)

An external collar contains and controls the flow of hot air and powder into a “cooling device,” actually a commercial bag-less vacuum cleaner with chilled air at the intake. Chilled air at –20 C combines with hot air at 200 C to lower air temperature to 50 C. The vortex in the canister then cools and separates micropellet powder from the air stream.

Initial research was done with HDPE and LDPE. For HDPE the extruder was set at 150 C. Hot air was tested at temperatures from 130 C, close to HDPE’s crystallization temperature, up to 160 C, above HDPE’s melt temperature. Airflow was tested from 345 cu m/sec, where the polymer thread starts to break up, to 730 cu m/sec, corresponding to air speeds of 55 to 120 m/sec. Maximum air pressure in the nozzle was 0.6 MPa. Screw speed varied between 1 and 20 rpm for throughputs of between 55 and 350 g/hr.

Different polymers seem to make different powder shapes and sizes, but all are consistent and rounded. HDPE makes micropellet powders that range in size from 65 to 400 microns and are smooth and lemon-shaped under a microscope with tails at one or both ends caused by the Rayleigh disturbances. LDPE makes micropellet powders that are slightly larger (169 to 505 microns), rougher and bean-shaped, sometimes without tails.

Osswald has since received a $50,000 grant from the University of Wisconsin (Madison Draper Technology Innovations Fund) to scale the prototype up and characterize the process better. Material testing will try to figure out what influences the breakup into droplets and model optimum process conditions for a variety of polymers. Simulation is being done using OpenFOAM, an open fluid dynamics software program developed at the Inter University Centre of Dubrovnik, Croatia (www.iuc.hr).

This diagram shows how the lab line at the Univ. of Wisconsin works. As melt exits the capillary tube, it’s stretched downward by high-speed hot air, and breaks into powder. Powder is cooled and separated in a bag-less vacuum cleaner with chilled air.

The initial focus is on PLA. This year researchers successfully made PLA micropellets, which are somewhat elongated like little worms. Powdered PLA, made by grinding, is currently available only from one supplier, ICO Polymers in Houston, a division of A. Schulman (www.icopolymers.com). ICO sells PLA in several screened sizes and in both amorphous and crystalline form.

Osswald also wants to be able to separate die and air temperatures. In the prototype the capillary tube in the die is used to guide the hot air, so air and die temperatures are linked. Having independent air and die temperatures might allow finer tuning with some materials, Oswald expects.

OTHER NEW MICROPELLET TECHNOLOGIES

There is another patented micro-droplet technology in the literature (German patent PCT/EP 2004/000506) belonging to Zapf Creation AG, a doll and toy maker in Rodental, Germany. Zapf’s patent for a “Method and Device for Producing a PVC-Free Powder that is Essentially Made of Plastic” describes extruding a curtain of polymer downward from a slot die, then breaking the curtain up into droplets using a supersonic air stream from a De Laval nozzle. The work was done ten years ago by inventor, Gerhard Barich, a professor from Munich University of Applied Sciences in Germany, to produce non-PVC compounds for toys. The patent describes making spherical micropellets 20 to 500 micron in size out of styrene ethylene butylene styrene (SEBS) rubber at 270-290 C along with other materials. So far it hasn’t been commercialized.

RTP Company, a compounder in Winona, Minn. (www.rtpcompany.com), recently commercialized another interesting approach to micropellets. They aren’t as small as powder, but they also target higher bulk density competing against ground powders. RTP’s patent-applied-for technology for “controlled geometry composite micropellets” (U.S. Pat. # 20100291388) extrudes a variety of strands with different cross-sectional geometries including circles, triangles, rectangles, and diamonds and pelletizes them in lengths of 1.2 to 2 mm.

RTP Company’s new “controlled geometry pellet” micropellets combine a mixture of cross-sectional geometries including circles, triangles, squares and diamonds. They reportedly fill a compression mold with less empty space than ground powders.

“When micropellets with a mixture of geometric shapes are poured into a mold, they stack with very little empty space, so you don’t have to overfill a compression mold,” says RTP market manager Eduardo Alvarez, one of the inventors. CGP (controlled geometry pellets) also reportedly wet out fiber better in compression molding than cryogenically ground powder. RTP commercialized CGP micropellets late last year primarily for high temperature resins. Strand pelletizing can be used for higher temperature polymers than underwater micropelletizing.

Conventional under-water micropelletizing dies are also making ever smaller micropellet sizes for rotomolding. Gala Industries Inc. in Eagle Rock, Va. (www.gala-industries.com) has made micropellets as small as 450 microns, where typically the smallest commercial micropellet size is 500 micron. Gala also invested in a full-scale rotomolding machine with multiple arms for comparison trials in its labs.

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How to Attack a Patent for 90% Less Suing

First, have a solid prior art case. If you do, there is a much less expensive way to get a patent revoked than litigation. “Even a small patent litigation case in court may run $1 million for each side,” says intellectual property lawyer Steven J. Grossman of Grossman, Tucker, Perreault & Pfleger PLLC in Manchester, NH (www.gtpp.com). Patent lawsuits cost both sides because it’s hard to get cost shifting, he adds, so even the winner will pay a lot.

The less expensive alternative is to ask the patent office to reexamine a patent. “USPTO reexaminations typically cost only about $100,000,” Grossman asserts, including around $2500-$8800 in fees to the USPTO and the cost of a patent lawyer. “They also have an extremely high ‘kill’ ratio,” he adds. USPTO reexaminations are successful for the challenger nearly 80% to 90% of the time (www.uspto.gov/patentsReexamination_operational_statistic_through_FY2011Q).

Patent office reexaminations have been highly successful for the challenger. As of mid 2011, “Inter partes” reexaminations (pie chart) cancelled 45% of patent claims, amended 43%, and confirmed 12%. Source: Grossman, Tucker, Perreault and Pfleger

Grossman introduced the process to a plastics audience for the first time at the Society of Plastics Engineer’s ANTEC conference in Boston in May (see May blog). His presentation on “Recent Procedures Introduced to Challenge Patent Grants at the United States Patent and Trademark Office” explains how it works. A CD of all ANTEC papers is available to non-attendees for $150 from the SPE (www.4spe.org).

USPTO reexaminations are intended to streamline the complaint process and reduce the burden on federal courts. They have been around in some form for 30 years, but are still little known and little used because of several limitations.

One limitation is that they can be based only on prior art, the same criteria the patent office uses to grant patents in the first place, specifically “prior written art consisting of patents or printed publications.” A patent office reexamination can’t use legal discovery or depositions the way a lawsuit could. So if a challenger’s issue is prior manufacture or sale of the technology, for example, or a suspicion that the patent holder misrepresented facts to the patent office, these arguments can’t be raised in a reexamination.

WHICH TYPE OF REEXAM TO USE?

The USPTO offers two types: “ex parte” and “inter partes,” which are quite different. “Ex parte,” the original form, was instituted in 1981 and can be used to attack any issued patent. “Inter partes” reexamination was authorized by Congress in 1999 and is limited to challenging patents filed after Nov. 29, 1999.

A bigger difference between the two is whether the challenger is involved. “Ex parte” means “without” the challenger involved. The challenger isn’t allowed to see or comment on the patent holder’s response to the prior art issue, which gives the patent holder the upper hand.

“It’s a little like firing a cruise missile without control,” comments Michael Brown of Brown & Michaels PC in Ithaca, N.Y. (www.bpmlegal.com), who hasn’t brought any patent office reexaminations himself, though others in his firm have. “Unless you have absolutely solid prior art, the examiner will examine the art you have cited and issue an office action. That office action goes to the patent holder, who then responds to it. If the patent holder can amend their claims, you have allowed the patent holder to keep their patent. It’s this lack of control that bothers some people,” notes Brown.

“Inter partes” reexamination means “between” the patent challenger and the patent holder and offers a more level field. The challenger can see the patent holder’s response and file comments on it in return. “The requestor is allowed to remain fully active in the proceeding and continue to raise arguments against the patent holder as the patent holder attempts to overcome the cited prior art,” Grossman explains.

Not surprisingly, both the overall success rate and patent “kill” rate for “inter partes” reexaminations are higher. Inter Partes Reexamination Certificates favor the challenger 88% of the time vs 77% for “ex parte.” “Inter partes” also cancels four times more patents—45% for “inter partes” vs 11% for “ex parte.”

In the first five years that “inter partes” reexaminations (black) were available, there were only 53 vs around 1700 “ex parte” requests (diagonal lines). Both are still far below patent office projections (vertical lines). Source: Grossman, Tucker, Perreault and Pfleger

The mixture of outcomes for the two types is also different. “Inter partes” certificates have cancelled patent claims 45% of the time, amended patent claims 43% of the time, and upheld them 12% of the time. “Ex parte” certificates, on the other hand, have cancelled patent claims only 11% of the time; amended them 66% of the time; and upheld them 23% of the time. So the patent survival rate for “ex parte” is nearly double that of “inter partes.”

The patent office projected 400 “inter partes” reexaminations in 2000, the first year they were available, and got 0. Growth has been slow even though they cost a fraction of the cost of litigation. Source: Grossman, Tucker, Perreault and Pfleger

It’s sometimes hard to pick clear winners because reexamination certificates can combine all three outcomes. “If the patentee has to amend his claims so that your product no longer infringes, you win, even if the patent survives the reexamination,” notes Brown.

Even with a mixture of outcomes, both types of patent office reexaminations are highly successful for the challenger in terms of either canceling or amending patent claims. The reason, intellectual property lawyers say, is that the USPTO is so over-loaded. It has a backlog of a year and a half of applications to review (695,086 applications as of June 2011) and only 6,775 examiners to review them, so a lot of patents get approved that shouldn’t have been.

One high profile example of a patent that probably shouldn’t have been is the so called “patent on a stick” (US Pat. # 6360693) for an Animal Toy that looks like a stick of wood. The patent, which certainly looked tongue-in-cheek, but wasn’t necessarily, caused such a furor among intellectual property lawyers after it was issued March 26, 2002, that the director of the USPTO asked for an “ex parte” reexamination.

This patent for a dog toy, known as “the patent on a stick,” was revoked in 2006 in one of the more famous “ex parte” reexamination cases, raising awareness of patent office reexaminations. Source: U.S. Pat. # 6360693

The inventor, Ross Eugene Long III, a California architect, had presented a bunch of ideas to a patent law firm and selected the flavored, potentially injection molded “stick” as the likeliest to be licensed. After Long initially received the patent, he hired an agent to identify prospective licensees. During the reexamination, he tried twice to amend the claims, but couldn’t. Four years later the claims were revoked. It turned out that there were a half dozen previous patents on stick-like items, mostly garden related, but close enough. Long didn’t appeal the decision because at that point he says he had already spent about $20,000 on the project. The unforgettable drawing may, however, have raised awareness of the reexamination process because requests to the USPTO definitely picked up after 2006.

Appeals are also different after “ex parte” and “inter partes” reexaminations. In “ex parte” cases only the patent holder has the right to appeal, not the challenger, a distinct disadvantage for the challenger. The patent holder can appeal either to the Board of Patent Appeals and Interferences in the patent office or to federal appeals court. In an “inter partes” reexamination, both the patent holder and challenger can appeal a decision first to the Board of Patent Appeals and Interferences and then to federal appeals court.

PTO reexaminations can also be concurrent with patent infringement litigation (in U.S. district court) with interesting twists. If the district court decides that a patent claim is valid, and the reexamination subsequently decides the claim was unpatentable, the patent will be cancelled. If, however, a final non-appealable court decision says the patent is invalid, that will stop the patent office reexamination.

During patent office reexaminations of either kind, an alleged infringer can keep selling his product with no immediate penalties until the reexamination certificate is issued and then only if the certificate validates the patent claims. By contrast, in patent infringement litigation, the court presumes the patent is valid, and the alleged infringer may have to stop selling the product if served with a preliminary injunction, Grossman points out. However, if an infringer ultimately loses in court, he still can be ordered to pay damages, which may go back either to the date of the patent grant or the date the suit was filed.

REEXAMINATION, ANYONE?

Activity in both types of USPTO reexaminations has been negligible for years. In mid 2011 a total of only 8129 Ex Parte Reexamination Certificates had been issued in all the 30 years that they have been available. Requests for “inter partes” reexaminations have been even more anemic. There were only 53 in the first five years that they were available, whereas the patent office had projected over 2000. There have still been only 253 Inter Partes Reexamination Certificates issued in all 11 years they’ve been available.

Lately, however, requests for patent office reexaminations are growing at last, presumably buoyed by recent successes for the challenger. Requests for “inter partes” reexaminations totaled 1061 in 2010 with 281 “inter partes” and 780 “ex parte.” Total requests in the first half of 2011 is 572with 180 “inter partes” and 392 “ex parte.”

Congress is currently also considering changing the regulations on patent office reexaminations to augment “inter partes” reexamination with “post grant review.” This would allow challengers to raise more issues against a patent than prior art. “In post grant review, it appears that one could attack the granted patent on the grounds that in addition to prior art arguments, the claimed invention is not supported by the disclosure, or that the claims fail on the basis that they are unclear in scope,” Grossman explains. That would remove a big limitation on the scope of reexaminations and should finally increase their use.

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