BEND RESEARCH, INC.

Company Information

Company Name
BEND RESEARCH, INC.
Address
64550 RESEARCH RD
BEND, OR, 97701
Phone
1 503-382-4100
URL
n/a
DUNS
n/a
Number of Employees
n/a

Award Totals

PROGRAM/PHASE
AWARD AMOUNT ($)
NUMBER OF AWARDS
SBIR Phase I
$6,805,457.00
114
SBIR Phase II
$24,166,074.00
60
Chart code to be here

Award List

  1. CLORINE-RESISTANT HOLLOW-FIBER REVERSE-OSMOSIS MEMBRANE ELEMENTS

    Amount: $500,000.00

    COMMERCIALLY AVAILABLE REVERSE-OSMOSIS MEMBRANES ARE CHEMICALLY ATTACHED BY CHLORINE. THUS, CHLORINATION CANNOT BE USED TO PREVENT BIOLOGICAL FOULING OF THE MEMBRANE ELEMENTS. WE PROPOSE DEVELOPMENT O ...

    SBIR Phase II 1984 ArmyDepartment of Defense
  2. SLUDGE RECLAMATION USING COUPLED-TRANSPORT MEMBRANES

    Amount: $99,761.00

    IN 1980 THE METALS AND ELECTRONICS INDUSTRIES GENERATED OVER SEVEN MILLION TONS OF HAZARDOUS WASTE AT A COST OF $100TO $400/TON. THESE SLUDGES, WHICH CONTAIN SUBSTANTIAL AMOUNTS OF MIXED HEAVY METALS, ...

    SBIR Phase II 1984 Environmental Protection Agency
  3. ONBOARD WATER GENERATION FOR MILITARY VEHICLES

    Amount: $154,683.00

    SUPPLYING ADEQUATE DRINKING WATER TO SOLDIERS ON ARID OR CONTAMINATED BATTLEFIELDS IS A FORMIDABLE PROBLEM. ONE POSSIBLE SOURCE OF WATER IS ENGINE EXHAUST; FOR EXAMPLE, DIESEL EXHAUST CONTAINS 1.1 POU ...

    SBIR Phase II 1985 ArmyDepartment of Defense
  4. OPTICAL RESOLUTION OF DL-PHENYLALANINE IN A MEMBRANE REACTOR

    Amount: $207,000.00

    PURIFICATION OF THE PRODUCTS OF AN ENZYMATIC REACTION FROM DILUTE AQUEOUS SOLUTION CAN BE ENERGY- AND EQUIPMENT- INTENSIVE. HOWEVER, TWO-LAYER MEMBRANE BIOREACTORS CONSISTING OF SANDWICHES OF PERMSELE ...

    SBIR Phase II 1987 National Science Foundation
  5. CONCENTRATION OF SYNFUEL PROCESS CONDENSATES BY REVERSE OSMOSIS

    Amount: $491,321.00

    LIQUID AND GASEOUS FUELS PRODUCED FROM COAL OR SHALE OIL, I.E., "SYNTHETIC" FUELS, WILL BE MAJOR SUBSTITUTES IN THE FUTURE FOR THE DIMINISHING SUPPLY OF PETROLEUM-BASED FUELS. A SIGNIFICANT PROBLEM IN ...

    SBIR Phase II 1984 Department of Energy
  6. SOLVENT-SWOLLEN MEMBRANES FOR THE REMOVAL OF H(2)S AND CO(2) FROM COAL GASES

    Amount: $499,816.00

    ACID GAS REMOVAL BY CONVENTIONAL ABSORPTION PRODESSES IS AN EXPENSIVE STEP IN THE PRODUCTION OF CLEAN FUELS FROM BOTH LOW- AND HIGH-BTU COAL GASES. MEMBRANE PROCESSES FOR ACID GAS SCRUBBING ARE COMPAR ...

    SBIR Phase II 1984 Department of Energy
  7. THIN-FILM-COMPOSITE GAS-SEPARATION MEMBRANES PREPARED BY INTERFACIAL POLYMERIZATION

    Amount: $474,382.00

    MEMBRANE GAS SEPARATIONS ARE ATTRACTIVE BECAUSE OF THEIR LOW OPERATING COSTS, A CONSEQUENCE OF THE ENERGY EFFICIENCY OF MEMBRANE PROCESSES IN GENERAL. HOWEVER, THE MORE WIDESPREAD USE OF MEMBRANE SYST ...

    SBIR Phase II 1985 Department of Energy
  8. REVERSE-OSMOSIS MODULE FOR SPACECRAFT WASHWATER RECYCLE

    Amount: $283,165.00

    EXTENDED SPACE MISSIONS REQUIRE EXTENSIVE RECYCLING OF WATERTO PERMIT FREQUENT WASHING AND BATHING OF THE CREW. REVERSEOSMOSIS (RO), OFTEN CALLED HYPERFILTRATION, PROMISES TO BE A UNIQUELY SUITED TECH ...

    SBIR Phase II 1984 National Aeronautics and Space Administration
  9. THE ULTIMATE OBJECTIVE OF THE PROPOSED RESEARCH IS TO DEVELOP BIOERODIBLE POLYMER-DRUG IMPLANTS THAT CAN BE USED FOR EITHER LONG-TERM SYSTEMIC OR LOCALIZED DRUG DELIVERY.

    Amount: $47,597.00

    THE ULTIMATE OBJECTIVE OF THE PROPOSED RESEARCH IS TO DEVELOP BIOERODIBLE POLYMER-DRUG IMPLANTS THAT CAN BE USED FOR EITHER LONG-TERM SYSTEMIC OR LOCALIZED DRUG DELIVERY. THE SPECIFIC AIMS OF THE PHAS ...

    SBIR Phase I 1984 Department of Health and Human Services
  10. A NOVEL MEMBRANE-BASED WATER RECLAMATION POST-TREATMENT UNIT

    Amount: $405,000.00

    FOR FUTURE LONG-TERM SPACE MISSIONS SPACECRAFT WATER RECYCLE SYSTEMS ARE NOW UNDER DEVELOPMENT. ONE WATER RECYCLE SYSTEM STUDIED BY NASA INCLUDES A REVERSE-OSMOSIS (RO) SUBSYSTEM THAT WILL PRODUCE REU ...

    SBIR Phase II 1986 National Aeronautics and Space Administration

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