SARAH WANG, P.E.

**** **** *** ****, ************, NC 27883

832-***-**** ad0tix@r.postjobfree.com

PROCESS ENGINEERING

PROFILE

M.S., Chemical Engineering

B.S., Chemical Engineering

Licensed Professional Engineer #114605

Project Management Professional (PMP) Registration # 394240349

Lean Six Sigma - IASSC® Certified Green Belt, ICGB #GR813000621SW

Change Management Specialist Certification

Over Fifteen years of diversified international experience in the Engineering sector

Well-qualified to contribute in Pharmaceutical environment from Lab, Pilot Plant to FDA-compliant Production, from conceptual to start up and commissioning.

Expertise in Bioprocessing, WFI, Pharmaceutical Product Design, Gene and cell therapy, Single Use Technology, Aseptic Processing, Fermentation processes, Solid Dosage, Fill & Finish, Technology transfer from R&D to GMP manufacturing, Troubleshooting Process Equipment and cGMP Facility Renovation and Expansion.

Proven capacity in lifecycle project management, initiating and implementing effective engineering projects.

Adept in Generic Drug Development, Process Optimization, Sanitary equipment design and 6 sigma Methodology

Record of promotion to assignments of increasing authority and responsibility.

Knowledgeable in full-life-cycle project and staff management.

Skilled presenter and facilitator.

Effectively interact with diverse groups and professionals at all levels.

Well-organized multi-tasker with strong detail orientation.

Proficient in SuperPro, SchedulePro, Pipeflo, Veeva, Blue Mountain, Kneat, Minitab, Trackwise, LIMS, Siemens Building Automation System, Emerson Delta V, PI Data Historian, Infor EAM, HYSYS, ProMax, ASPEN PLUS, Aspen Dynamic, PRO II, HTRI, ASPEN EDR, ASPEN PIMS, ChemCAD, AutoCAD, Plant 3D, HPLC, Mass Spectroscopy, Ultraviolet–Visible Spectroscopy, Immunoassay Techniques, Solid-State Nuclear Magnetic Resonance Spectroscopy, SAS Programing, Pipesim, OLGA, PVTSim, FlowManager, PLC, Matlab, C++, VB, SAP, BIM 360, Bluebeam and Microsoft Office.

Published author (see below).

PROFESSIONAL EXPERIENCE

• Lead process mapping and continuous improvement activities of the production line.

• Provide statistical analysis processes.

• Participate in engineering/production functions to achieve overall objectives of the plant.

• Provide engineering activities regarding the innovation, design, purchase, fabrication, installation, start-up, and validation of production machinery and processes and defining and optimizing Bills of Materials and Routings

• Apply lean methodology to the job and follow cGMP.

• Troubleshoot Process Equipment and Incident Investigation.

• Retained to develop design basis, conceptual and advanced process design and feasibility study/simulation.

• Demonstrated capacity in computer aided simulators including SuperPro, SchedulePro, HYSYS, ASPEN PLUS and PRO Max to calculate heat/mass balances and physical properties.

• Aided in ICH Q8-Q11, ASME BPE, ASTM E2500, ASTM E3051-16, NFPA, API, ISO 11137, ISO13485, GAMP Standards and European Codes. Extensive knowledge of 21 CFR 11 requirements.

• Initiated Process Flow Diagrams (P.F.D.), Piping Instrumentation Diagram (P&ID) and defined control strategy.

• Gained solid thermal design/sizing background for heat transfer equipment.

• Successful in plant commissioning, Risk Assessment, HAZOPs and PHAs for multiple processes. Fresenius Kabi, Wilson, NC 2023-Present

Senior Technology Transfer Leader

• Managed all projects related to new products, product modernization and all product transfers for the Standard Solution plant and the Syringe Plant.

• Communicated Standard Solution plant and Syringe Plant issues and tasks with the project team with respect to scaling up processes, new equipment and procedures, equipment and process validation, manufacturing of development, stability, and product validation batches.

• Authored 0.9% NaCl Exhibit & Commercial, Lactated Ringer’s, 0.45% NaCl, 5% Dextrose, Dex-NaCl Combos, Line3&4 Fill line, Terminal Sterilization and Packaging line master batch records and protocols for the manufacture of development, stability, and validation batches. Successfully translated development findings into manufacturing processes.

• Identified and implemented best practices and procedures designed to provide robust manufacturing processes.

• Technically assessed changes in manufacturing through appropriate review of documentation and testing results. Reported changes through risk assessments. Conducted Manufacturing Risk Assessment for Dexamethasone Sodium Phosphate, Dilaudid (Hydromorphone HCl), Heparin Sodium, Ketorolac Tromethamine, Metoclopramide, Midazolam, Morphine Sulfate and Ondansetron, etc to identify the risks that exist within the manufacturing process based on the critical process parameters for the products. Developed Control plan and response plan and conducted CAPAs.

• Provided technical support for Investigations, Action Plans and Material Change Requests, etc. as required. Generated innovative solutions to solve difficult problems that impacted multiple disciplines.

• Developed and executed investigative studies and validation protocols for Lactated Ringer’s, 0.9% NaCl Exhibit & Commercial, 0.45% NaCl, 5% Dextrose, Dex-NaCl Combos, Labetalol and Sugammadex, etc from Formulation, Filling & Sterilization and Packaging for the Standard Solution plant and Syringe Plant. Successfully Implemented Stratified sampling to minimize the Possibility of errors and ensured its capability of showing causes of variation.

• Managed routine departmental assignments such as project time tracking, APQRs schedules, Product Modernization and Continue Process Validation monitoring. Developed CPV report for Midazolam, Dexamethasone Sodium Phosphate, Dilaudid (Hydromorphone HCl), Heparin Sodium, Ketorolac Tromethamine, Metoclopramide, Morphine Sulfate and Ondansetron product family, created Minitab models and Successfully interpreted the charts for the Dexamethasone Sodium Phosphate, Dilaudid (Hydromorphone HCl), Heparin Sodium, Ketorolac Tromethamine, Metoclopramide, Midazolam, Morphine Sulfate and Ondansetron critical quality attributes. Identified trends and patterns, Analyzed and interpreted data and results, Identified solutions to the problem at hand for the Dexamethasone Sodium Phosphate, Dilaudid (Hydromorphone HCl), Heparin Sodium, Ketorolac Tromethamine, Metoclopramide, Midazolam, Morphine Sulfate and Ondansetron prefilled syringes. Performed Statistical Analysis and ensured process capability Cpk>=1.33 and evaluated X Chart for 7 consecutive points increasing and decreasing, any new data points outside the UCL/LCL, etc.

• Optimized heating, sterilizing and cooling phases of the Terminal Sterilization of Prefilled Syringes and standard solutions. Successfully implemented adequate supporting pressure overlay during the different phases using sterile filtered compressed air to ensure the integrity and dimensional stability of the container and adjusted the pressure individually and prevented deformation, container breakage, and stopper movement.Slashed $5M cost.

• Maintained the flow of the steam/air mixture at all times and ensured appropriate loading pattern, all requirements for an efficient and safe sterilization as well as the desired degree of drying are met. Slashed $2M cost.

• Successfully resolved the Integrated Bag filling machine Left Hand Side not starting issue due to the camera system/ vision system misalignment and Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and identified the root cause the screw came loose during cleaning and the camera is not scanning the bar code and the variable data. Developed, tested, and implemented solutions and retightened the screws and realigned the camera and put the production online. Updated the SOP and Monitored key factors and maintained the gains. Slashed $2M cost.

• Successfully resolved the Integrated Bag filling machine Right Hand Side left excessive ink on the freeflex® bag issue. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and Identified key root causes for process variation such as the compression spring on the printer was broken and the roller was hanging lower than expected. Developed, tested, and implemented solutions and replaced the compression spring. Updated SOP and PM schedule implemented the correction and monitored key factors and maintained the gains. Slashed $5M cost.

• Successfully resolved the Filler partial Fill Issue by adjusting the Fill Level With the Valve Spacers. Slashed $2M cost.

• Successfully resolved the filling nozzles were clogged and dosing time error for the valve issue. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and Optimized the pump settings to adjust the level of fluid retraction in the needle and successfully reduced the rate of formulation drying. Carefully selected formulation excipients and lower the viscosity the product to minimize the deviation in filling accuracy, product loss and extended interruption time during a filling operation this is to lower the viscosity of a high concentration drug product. Analyzed needle material and selected the needles manufactured from hydrophobic materials allow the liquid plug to form away from the needle tip to slow down formulation drying rates and prevent clogging. Updated the SOP and Monitored key factors and maintained the gains. Created $10M operation value.

• Successfully resolved Line 3 Integrated Bag filling machine right hand side stopped and the vacuum pad is not grabbing the freeflex bags issue. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and identified the root cause line 2 vacuum pad installed to line 3 and the vacuum pad was not centered and Developed, tested, and implemented solutions and checked the vacuum pressure and swapped out the vacuum pad, put the production online. Slashed $1M cost.

• Successfully resolved the Storage Tank 220-ST-032 Agitator speed oscillates from 334rpm to 448rpm while the set point is 366rpm issue. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and Ensured that the proximity sensor cable is not damaged, and that it is separated from high-power spindle/axis/pump cables. Made sure the connectors and pins for the proximity sensors are not contaminated. Made sure the pins have not backed out of the connector. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and identified the root cause that the proximity sensor malfunction due to improper installation, the sensor is placed too deep in the flange. Developed, tested, and implemented solutions and Replaced the proximity sensor and tuned the controller. Monitored key factors and maintained the gains. Slashed $3M cost.

• Successfully resolved Line 3 Over-wrapping Machine thermoforming station malfunction issue and the measurement for the overwrap seam of the freeflex® bags were out of spec and the upper and lower spec limit is 4.00mm to 5.00mm and the measured value is 5.20mm. The thermoforming station heats up the film and pushes it into the cavities to form the molds. The bottom film is pushed against a heating plate on top of the forming station using pressurized air. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and identified the root cause for process variation that unable to control the heating temperature and air pressure during the power glitch and it caused more expansion on the film. Successfully identified dimensional Inconsistencies for the Line 3 and 4 cavities. Developed, tested, and implemented solutions and Adjusted operation parameters and put the production online. Slashed $4M cost.

• Successfully prompted a re-analysis of measuring systems to reduce the Calcium, Sodium and Potassium assay variations compared to Friedberg, Germany and Halden, Norway for the Lactated Ringer for new product transfer and selected gage R&R to ensure the measurement system is accurate and precise. Slashed $5M cost.

• Successfully resolved Post use finial bio-burden filter integrity test failed with the Forward-flow test for the 5% Dextrose and 0.9% Sodium Chloride issue. Utilized Forward-flow test for the Hydrophilic membrane integrity tests since it is more accurate than the bubble-point method and it injects a constant amount of air at a specific flow rate through the wetted filter. The volume of air displaced from the upstream side to the downstream side is continuously measured. If the volume maintains a rate below a certain limit, the filter is integral. The forward flow limit is 12.0 mL/minute(4 in parallel) using air at a test pressure of 40.00 psig when the filter is fully wetted. The measured flow for the Post use bio-burden filter is 56.9 mL/minute. Checked the Hydrophilic sterilizing filter damage in the form of membrane blockage, cracks, and changes to pore structure during use. Checked Over-pressurizing the membrane and it can result in filter damage and invalid data, particularly after it has been used and may be clogged. Implemented the Best practice of performing the test at a slow and steady rate to make sure the correct amount of pressure is applied. Ensured proper temperature control since if tested at a higher temperature, the filter manufacturer should be queried for values calculated based on that temperature. Checked Test Set-up and Execution. Re-wet and re-test prior sending it back to the manufacture since the filter can sustain damage during the shipment. Supported decision-making based on the comprehensive information extracted from a full exploration of available data and the only way to guarantee the performance of sterility filtration is to conduct integrity tests on the Post use finial bio-burden filter, before and after use, even though Stratified samples were collected from each cycle for sterility testing. Slashed $5M cost.

• Successfully structured cleaning procedure to ensure the effective cleaning of equipment for the Standard Solution(WISSL) plant and Syringe Plant. Mapped the process and identified potential sources of contamination and variables that may affect the cleaning effectiveness and performance. Identified the contamination risks and established the appropriate corrective measures and associated controls needed to be put into place and conducted pre-trial tests on the worst-case product. Created $2M operation value.

• Successfully added insulation for the steam condensate pipes within 7 feet of the floor in the mixing bay in the tank room for personnel protection per OSHA 1910.261.

• Ensured dextrose solubility at the mixing temperature to fully mix 10% dextrose in a smaller mixing tank(6000L) for the storage tank working volume batch quantity of 31,500L.

• Successfully Implemented Kaizen for the Standard Solution(WISSL) plant and Syringe Plant and resolved compressed air and the steam shared the same header, while cooling the mixing tank, unable to start SIP for the storage tank issue and Added another set of valves and piping so the storage tank and mixing tank can have its own dedicated clean steam and clean air supply to resolve the unable to start SIP for the storage tank while the mixing tank is in cooling phase(using the compressed air) issue and eliminated 8hrs waiting time per batch and increased OEE by 30%. Slashed

$10M cost.

• Successfully resolved not realizing the film is expired till the installation was completed issue and Utilized Poka-yoke lean tools to do it right first time and recommended implementing the Electronic Batch Records to scan the bar code from the pick list first before it can proceed to the next step and make it impossible to make a mistake. Ensured 21 Code of Federal Regulations (CFR) Part 11 is met from a compliance standpoint and improved data integrity and accuracy, streamlined processes. Optimized processes yields, improved resource management, improved inventory management, and reduced material losses-all of which positively impact the operation’s bottom line. Improved time-to-market. Real-time information access also created opportunities to speed up processes throughout the production cycle. For example, gauge data can be automatically collected versus requiring a worker to physically walk to each gauge and record their readings. The ability to collect and review process information also allows one to identify and eliminate unnecessary tasks, such as redundant material checks. Eliminated the time and costs associated with storing physical documents. Dynamic EBRs can expand on those savings, by using automated QA functions to reduce the cost of researching process deviations, for example and MES with EBRs reduced the likelihood of human errors. The ability to create enforceable workflows, for example, helps ensure workers follow established processes and procedures, which can prevent production or recording errors that lead to wasted product or product recalls. Slashed $10M cost.

• Successfully resolved Loading robots flashing, De-Stacking robots flashing and Stacking robots flashing issue with Event Message 38101, SMB Communication failure, the system went to system failure state and lost its calibration information on TLS line 3 and A transmission failure has been detected between the axis computer and the serial measurement board on measurement link 1 in drive module 3. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and identified the root cause Cable connections were loose from the movement. Developed, tested, and implemented solutions and Retightened the cable connections and restored calibration information. Updated the SOPs and Monitored key factors and maintained the gains. Slashed $1M cost.

• Successfully resolved Stacking robot arm jammed issue. Upon restarting, robots go to home position(destacking and restacking the trays) and the Stacking robot arm was jammed during reset. Implemented RCA tools such as Ishikawa diagram, cause effect matrix and 5 Why’s technique, etc and identified the root cause that one of the trays was bent caused by thermal stress due to the heat in the sterilization and robot arm grabbing action and the robotic arm is jammed and unable to grab the tray in the stacking process. Developed, tested, and implemented solutions and installed new trays and put the production online and updated the PM schedule and Monitored key factors and maintained the gains. Slashed $3M cost.

• Initiated Continued process verification (CPV) for cleaning validation (CV) program to maintain the validated state of cleaning for the Standard Solution plant and Syringe Plant.

• Successfully Identified inline monitoring to compensate for the Micro sample incubation time so it doesn’t exceed the hold time.

• Retained to update the gowning SOP and installed mirrors and posted example gowning pictures in the personnel airlock to ensure gowning integrity before entering the cleanroom. Suggested to provide plastic covers and wipes for electronic devices in the airlock. Ensured the Lifecycle of the clean garments to be confirmed to reduce the risk of contamination.

• Corrected the no medium size scrubs in the personnel airlock and the smallest scrub is large and often not available issue and ensured a good fit for sterile garment and reduced contamination risk; prevented instances as sterile clothing that is too big may accidentally touch surfaces while clothing that is too small may break during use. Improved the fit and ensured the sterile clothing is available in a wider range of sizes so people can choose different sizes to better match their proportions. Suggested Integrated clothing, such as clothing that features an integrated hood to make the Syringe building gowning process simpler and easier.

• Provided information and documentation needed for regulatory submissions and responses as required.

• Served as Plant liaison for manufacturing processes to other departments within the site, other business units within the company, and marketing units. Served as the plant point of contact for channeling all manufacturing related questions and issues for resolution.

• Assisted in the training of new employees to the Technology Transfer department Kerry Group, Rochester, MN 2022-2023

Process Engineer

• Developed Process Improvement Plan with recommended short- and long-term solutions.

• Identified and analyzed existing processes, procedures and systems to identify areas for improvement in logistic operations

• Developed and implemented strategies to improve efficiency, productivity, and quality of operations

• Conducted process assessments, mapping, and documentation to identify bottlenecks and inefficiencies

• Collaborated with cross-functional teams to streamline processes and improve operations

• Developed and implemented process metrics and KPIs to track progress and identify areas for improvement

• Conducted root cause analysis to identify underlying issues and recommend solutions

• Designed and implemented process improvement initiatives using Lean Six Sigma methodologies

• Provided training and support to teams to ensure successful implementation of process improvement initiatives

• Integrated Process, Project Management, packaging improvements and sanitary design for food manufacturing.

• Successfully led capital and continuous improvement projects through accurate project forecasting and budgets, process optimization, equipment procurement, scheduling, integration, installation, start-up and successful project closure.

• Provided process troubleshooting support, made technical recommendations, answered technical inquiries, improved process engineering tools, and developed process procedures.

• Provided support to and carry out studies (Risk Assessment, PHA, HAZOPs and Relief Systems, etc.) to improve plant safety, reliability, and economics.

• Developed PFDs and P&IDs for the Liquefiers, fermentors, culture centrifuge, pasteurizer, evaporator, Spray dryer, sterile air system, autoclaves, Dry blend and packaging, culture packaging, liquid packaging, boiler, DA tank and steam, condensate systems, etc

• Performed Data Gathering/Analysis of existing Non-Conformance.

• Specified YSTRAL Conti-TDS powder induct, wet and disperse machine to not only wet, but disperse the powder in the liquid under vacuum, avoided agglomeration, optimized the result with a better breakdown, higher raw materials efficiency and higher product quality. Created $5M operation value.

• Successfully commissioned powder fluidiser FSA-5 to mechanically loosen the powder with rotors, which already produces a mixture and results in a continuous powder flow. Equipped the powder fluidiser with the Fill level monitor, Fill level probe, Oscillation aerator, Aerator nozzle BD 100, Suction hose aeration and Aeration mushroom, etc. Created $1M operation value.

• Recommended vertical Jetstream mixing and Slashed 90% of the process time for the Liquefier 4. Improved the Conventional agitators and stirrers which create a horizontal rotation of the liquid and the inertia of the rotating media which hinders the vertical mass exchange. Ensured homogeneous mixing. Create $5M operation value.

• Improved Liquefier 4 ergonomics and minimized risk and maximized productivity and installed additional safety grating on the dedicated charge ports for extra protection and to make it easier for operators to dump bags of dry raw material into the Liquefier.

• Specified UL-listed operator controls in a NEMA 4X stainless steel enclosure with 3R fan shrouds, variable frequency drive, All interior and exterior surfaces of the blenders made of stainless steel, polished to 150-grit sanitary finish.

• Implemented SIP process to reduce contamination through out the plant. Articulated critical requirements associated with SIP include proper steam distribution, noncondensable gases removal, and continuous condensate elimination. Implemented good engineering practices, adequate piping design, steam traps, valves, and monitoring instrumentation to ensure SIP integrity. Slashed $5M cost.

• Specified hydrophobic materials such as PTFE for the Donaldson sterile air filter to prevent blockage by humidity during use. Provided correct drainage of condensate for the filter housing to prevent condensate accumulating on the membrane during SIP, producing blind filters(the steam no longer passes through the membrane), and incorrect sterilization.

• Successfully installed temperature probes in the coldest points, the drain points to monitor the SIP process and added steam traps downstream of the bleed valves allowing condensate removal, reducing the steam flow rate, and minimizing the pressure differential across the filter. Slashed $2M cost.

• Successfully implemented sterile air to pressurize the system and completely purge the condensate through the bleed valves to prevent vacuum and ensured the pressure gauges indicating a positive reading in all parts for SIP integrity, also allowed the cooling of the equipment and filter for post- SIP integrity testing.

• Successfully installed Tetra pack BM40 centrifuge and utilized hermetic seals to prevent intake of destructive air. Simplified and accelerated the centrifugation steps in the workflow. Enabled remote monitoring of the device, notification of alarms and events through iFix. Introduced density control program. Slashed $5M cost.

• Performed Heat transfer calculations, Heat exchanger selection, LMTD calculation, tube and Shell sizing, required number of tubes options calculation, tube pitch selection, optimized the placement of the fluid, specified the TEMA class and tube materials to handle thermal expansion, avoided internal gasket joints, implemented easy to replace bundle and minimized the contamination of the tube fluids with higher pressure shell fluids. Slashed $2M cost.

• Specified Gemu utility valves, SPX, GEA process valves, etc to assure the Safe Handling of the nutritional products. Created $5M operation value.

• Prepared the Air permit for the facility to meet state and federal air regulations, and to minimize the impact of air emissions on people and the environment.

• Performed dust collector calculations, duct work sizing, initiated hood certifications, minimized footprint and prolonged the filter life, etc. Slashed $1M cost.

• Successfully Resolved R3 Cold cyclone diverter valve caked up causing production to shutdown issue and implemented the immediate solution to COP the R3 Cold cyclone diverter valve and put the production online and developed CAPAs to improve the PM plan on the Desiccant Wheel to dehumidify and cool the process air to the cold cyclone to mitigate the plugging. Verified the ability to effectively clean and wash the product contact and sealing areas of R3 Cold cyclone diverter valve with the use of specifically designed CIP devices was compromised and integrated automated, dedicated wash active devices (fitted with cruciform discs to maximize the washing surface) within specific cold cyclone wash stations, introduction of high integrity washing mechanisms. Slashed $2M cost.

• Successfully Resolved fermentor R304 and R102 contamination issue and identified the Root cause that the cask feeding to the seed fermenter R304 was contaminated and the cask sample result wasn’t obtained till the 28,000 gallon fermenter R102 completed fermentation(10hrs) and went into evaporation step because the current plating system incubates at 20-25 C for 2-3 days and more than 98% of the microbes in the world do not form colonies and there is no ONE UNIVERSAL bacterial or fungal SELECTIVE agar plate that will allow the growth of all bacteria or all fungal strains such as the 5 genus species of fungal strains implicated in powderly mildew DO NOT plate at all and recommended to implement real time quantitative polymerase chain reaction (qPCR) and Raman technology to prevent reoccurrence. Slashed $3M annual cost.

• Successfully resolved the First floor conference room extremely cold issue and replaced the defective control board for the reheat coil relay for the first floor conference room.

• Recommended Citric Acid in lieu of Nitric acid for CIP since Citric Acid offers a safer, more environmentally friendly alternative to nitric acid. Citric acid is an organic acid that comes from citrus fruits like oranges, and as such is safe for employees to handle. Fumes from citric acid are not toxic and not harmful to the atmosphere, especially when processing infant formula and saved thousands of gallons of water and resolved the Nitrate level too high in the infant formula issue. Slashed $2M cost.

• Resolved Lumaco butterfly valve malfunction issue and identified the Root Cause that the moisture in humid air, air pollutants (atmospheric corrosion), and direct contact with water and CIP solution caused electrical traces in a printed circuit board inside of Lumaco butterfly valve to start corroding and the damaged the printed circuit board which mechanically supports and electrically connects electronic components using conductive trace lines, pads and other features etched from copper sheets laminated onto a non-conductive substrate and made from glass reinforced plastic with copper tracks in the place of wires, where the components are fixed in position by drilling holes through the board, locating the components and then soldering them in place and the copper tracks link the components together forming the circuit. Slashed $2M cost.

• Optimized the butterfly valve seal to perform to its full potential, Considered the Hygiene certifications, Multibarrier sealing and Temperature and pressure extremes to provide the effective configuration.

Contact this candidate