Multi-Stage Activated Biological Process (MSABP™)Eliminates Excess Sludge

1. Multi-Stage Activated Biological Process
(MSABP™)
Eliminates Excess Sludge
DAVE LAUER, P.E.
VP – SALES & MARKETING
Revisions by JACK AKIN, PE, MS
EMC-Engineers/Scientists, LLC

2. Topics of Discussion
 MSABP basics
 Evolution of the process
 Principles, design and performance of the
process
 Equipment scope
 Case histories
 Economic advantages

3. What is MSABP?
 Attached growth biological wastewater treatment process
 Multiple biological selectors in series
 Produces environment for the creation of naturally occurring microbial
food chains
 Whereby the organisms that reduce the organics are in turn
consumed by higher level organisms, termed “vulture filtrators”, and
removed from the flow train.
 Effectively eliminates pollutants in wastewater
 Does so without the generation of waste sludge (biosolids) common in
other biological processes
 Results in substantial capital and operation cost savings

4. Aeration Clarifier
TYPICAL ACTIVATED SLUDGE PROCESSTYPICAL ACTIVATED SLUDGE PROCESS
Aeration Clarifier
Effluent
Return Sludge
Mixed
Liquor
Screened
Degritted
Influent
Waste Sludge

5. MULTI-STAGE ACTIVATEDMULTI-STAGE ACTIVATED
BIOLOGICAL PROCESSBIOLOGICAL PROCESS
(MSABP(MSABP®®
))
Screened
Degritted
Influent
Effluent

6. • Custom designed process with pretreatment consisting of fine screening, and
grit removal
• Removal of inerts creates the required environment for the MSABPTM
reactor
• Process is based on spatial microorganism successions and trophic chains
• Provides for conditions in which organics are consumed by primary
microorganisms while the primary organisms are later consumed by higher
order predatory microbes.
• Process utilizes naturally occurring microbial food chains to reduce excess
sludge
MSABPTM
PROCESS

7. MSABP COMPLIES WITH
GLUMRB STANDARDS
• BOD LOADING PER UNIT VOLUME
• AERATION SYSTEM AND BLOWER
SIZING BASED ON STANDARDS FOR
BOD and NH3 DEMAND
• PROCESS EFFICIENCY

8. • The MSABP is an attached growth
process based on selector technology and
the creation of microbial food chains, where
the organisms that reduce the organics are
in turn consumed by higher level organisms,
termed predatory microbes, and removed
from the flow train.
• The hyper plug flow scheme and attached
growth technology produces a high quality
effluent in a simple, easy to operate
package.
• With the MSABP, there is reduced excess

9. Multi-Stage Activated
Biological Process
(MSABP™)

10. Who is Aquarius?
 A collection of engineers
and scientists
 250 years combined
wastewater treatment
experience
 Proprietary processes and
equipment
• MSABP
• ELCAT
• Diffused Aeration
 Offices in
• Port Washington, WI
• Israel

11. Who is EMC?
• A group of civil, environmental and
structural engineers and scientists
• Wastewater treatment systems
designers with over fifty years of
collective experience specific to
MSABP technology
• Offices in Medford and Jacksonville,
Oregon
• In professional cooperation with
Aquarius
- Engineers/Scientists, LLC (a BioScape Technologies Affiliate)
Environmental
Management
Consultants
Grants Pass * Jacksonville * Medford, OR
Ph: 541-474-9434, Ext. 1 * Fax 541-727-5488
bioscapetechnologies@charter.net, emc@emcengineersscientists.com
http://wwwemcengineersscientists.com

12. Tim Bossard, is a professional Civil
Engineer, is well acquainted with all
aspects of wastewater system and site
development design, and is the
structural authority with respect many
BioScape projects.Tim has over 35
years of civil and structural
engineering experience.
Jack Akin, is an Environmental
Scientist and professional
Environmental Engineer, and, as the
foremost domestic expert on the
biochemical processes associated with
BioScape treatment systems, works as
part of this team to provide the best
service available.

13. ►Dr. Efim Monosov, Chief Technical OfficerDr. Efim Monosov, Chief Technical Officer
 Chair of Civil Engineering, Leningrad University,Chair of Civil Engineering, Leningrad University,
RussiaRussia
►Developed ELCAT as part of doctorateDeveloped ELCAT as part of doctorate
studiesstudies
 Electro-Catalytic treatment of non-Electro-Catalytic treatment of non-
biodegradable wastewaters, and inorganicbiodegradable wastewaters, and inorganic
wastes such as herbicides, dyes, phenolswastes such as herbicides, dyes, phenols
►Established Elif Technology Ltd in 1994Established Elif Technology Ltd in 1994
►Developed MSABPDeveloped MSABP
 Biological treatment of municipal and industrialBiological treatment of municipal and industrial
wastewaters w/o waste sludge generationwastewaters w/o waste sludge generation

14. TechnologyTechnology
DevelopmentDevelopment
 MSABP utilized dispersedMSABP utilized dispersed
media initially with limitedmedia initially with limited
resultsresults
 Difficult to control biomassDifficult to control biomass
 First generation media usedFirst generation media used
successfully in industrialsuccessfully in industrial
applicationsapplications
 First applied in 1997First applied in 1997
at 30,000 GPD foodat 30,000 GPD food
oil processor foroil processor for
pre-treatmentpre-treatment
 Continued research lead toContinued research lead to
development of modern daydevelopment of modern day
media and processmedia and process

15. Industrial & Municipal ApplicationsIndustrial & Municipal Applications
….and No
Waste Sludge

16. MSABP Process
 Custom designed process
with pretreatment consisting
of non-biodegradable
removal
 Removal of non-biodegs
creates the required
environment for the MSABP
reactor
 Process is based on spatial
microorganism
successions and trophic
chains
PrimaryPrimary
VultureVulture
PrimaryPrimary
PrimaryPrimary

17. MSABP Process
 Provides for conditions in
which organics are
consumed by primary
microorganisms while the
primary organisms are later
consumed by higher
vulture filtrators
 Process utilizes naturally
occurring microbial food
chains to eliminate waste
sludge
PrimaryPrimary
PrimaryPrimary
PrimaryPrimary
VultureVulture

18. Oxidation and Synthesis:Oxidation and Synthesis:
Organic Matter + OOrganic Matter + O22 + Nutrients + Bacteria+ Nutrients + Bacteria
COCO22 + H+ H22O + (New Bacterial Cells) + EnergyO + (New Bacterial Cells) + Energy
Principal of MSABPPrincipal of MSABP
 Mass quantity of new cells (biomass) produced in aMass quantity of new cells (biomass) produced in a
stage will be lower than mass quantity of raw organicstage will be lower than mass quantity of raw organic
material oxidized in the stagematerial oxidized in the stage
 Energy transferred to the next trophic level results inEnergy transferred to the next trophic level results in
only a fraction being converted to new biomass theonly a fraction being converted to new biomass the
rest going to metabolic processesrest going to metabolic processes

19. Principle of the Process

20. Principle of the ProcessPrinciple of the Process
DecreaseinBiomass
DecreaseinBiomass
MassMass
of Finalof Final
ConsumersConsumers
Mass ofMass of
IntermediateIntermediate
ConsumersConsumers
Mass ofMass of
Primary ConsumersPrimary Consumers
Mass of PrimaryMass of Primary
ProducersProducers
DecreaseinEnergy
DecreaseinEnergy

21. Municipal ApplicationsMunicipal Applications
 ConventionalConventional
 DevelopmentsDevelopments
 SchoolsSchools
 ParksParks
 RetrofitsRetrofits
 NitrificationNitrification

22. Industrial ApplicationsIndustrial Applications
• FoodFood
• ChemicalChemical
• PharmaceuticalPharmaceutical
• PetrochemicalPetrochemical
• CosmeticCosmetic
• TextileTextile
• SlaughterhouseSlaughterhouse

23.  Bioreactor is divided intoBioreactor is divided into
8-12 stages8-12 stages
 Each cell contains aEach cell contains a
different and progressivelydifferent and progressively
designed food chaindesigned food chain
environmentenvironment
 Proprietary submergedProprietary submerged
fixed film media is used infixed film media is used in
each stage to provide higheach stage to provide high
bacteria density andbacteria density and
substrate contactsubstrate contact
 Media “stabilizes” desiredMedia “stabilizes” desired
organisms to provide highorganisms to provide high
removal efficiencies withremoval efficiencies with
negligible net sludge yieldnegligible net sludge yield

24. MSABP Design
Sizing Criteria
 Based on flow, 16-24 hours hydraulic retention time
– Dependent on level of treatment required
– Longer HRT for higher efficiency treatment
 Based on BOD5 loading < 40 #/d/kcf at 8-10°C
– Municipal typically < 15 #/d/kcf at 8-10°C
 8-12 stages
– Dependent on level of treatment required

25. Stage 1: Logarithmic Growth
 Absorption of dissolved organics by
organisms on the fixed growth media
 Logarithmic biomass growth in a short period
of time
 Carbon adsorption relative to mass of
microorganisms and oxygen
 Significant BOD5 reduction in this phase

26. Stage 2: Declining Growth
Complex oxidation process begins
thereafter with three kinds of reactions
– Biomass synthesis
– Endogenous respiration
– Nitrification-denitrification

27. Stage 3: Endogenous Phase
 Oxygen demand decreases in later stages of
the process
 Microorganisms are assimilated by higher
order organisms in the food chain
 Massive destruction of sludge mass occurs
 Process minimizes the “sludge” remaining in
the effluent with the only “sludge” leaving the
system is the TSS meeting permitted limits

28. Municipal MSABP Performance
MSABP Dissolved Oxygen Gradient
0.2
0.6
1
1.5
2
2.7
3.4
4.1
4.6
4.8
4.9 5
0
1
2
3
4
5
6
Stage
#1
Stage
#2
Stage
#3
Stage
#4
Stage
#5
Stage
#6
Stage
#7
Stage
#8
Stage
#9
Stage
#10
Stage
#11
Stage
#12
MSABP Stages v.s DO
DO,ppm
DO, ppm

29. Municipal MSABP Performance
MSABP Kinetic
0
50
100
150
200
250
2 4 6 8 10 12 14 16 18 20 22 24
HRT, hours
Concentration,ppm
BOD
TSS
NH4

30. Aquarius MSABP Scope of Supply
 Inert removal
 Diffused aeration
 Fixed growth capture media
 Aeration blowers
 Instrumentation
 System process controls

31. Inert Removal
 Removal of inert material
 Pretreatment screening
and grit removal
 Fine screen, 1 mm
openings
 Standard grit removal for
municipal applications
 Alternative grit trap or
septic tank pretreatment

32. Mechanical Purification
 Depending on characteristics,
options range from simple
settling tanks to mechanical
purification systems for
elimination of sand and coarse
mechanical impurities with
settling velocity exceeding 20
mm/s (about 4 fpm).
 Various designs for bar
screening configurations exist to
remove other non-organic
materials.

33. Diffused Aeration System
 Fine or coarse bubble
diffused aeration
 Oxygen provided to
satisfy process demand
in aerobic cells
 Mixing agitation to
control biomass film on
media

34. Fixed Growth Media and Frames
 Polyamide &
polypropylene material
 Ultra high media
surface area
 Uniform density to
support population
 Support frames are 304
stainless steel
 Integral rack covers or
basin covers

35. Aeration Blowers
 Duty and standby
blower configuration
 Positive displacement
typical
 Centrifugal for larger
flow applications

36. Instrumentation & Control
 Instrumentation
– Dissolved oxygen
 Control
– Overall oxygen gradient
– Blower output feedback

37. Influent Effluent
Flow(gpd)
210,000
---
HRT(hrs) 16 ---
BOD(ppm) 350 < 15
TSS(ppm) 400 < 20
NH3(ppm) 70 < 1
Yavne WWTP

38. Affidavit & 1 Year Data

39. Influent Effluent
COD(ppm) 1,000 <60
BOD(ppm) 450 <10
TSS(ppm) 250 <10
NH3(ppm) 100 <1
TN (ppm) --- < 5
JH Ranch, Etna, CA
45,000 GPD

40. Influent Effluent
Flow(gpd) 5,000 ---
HRT(hrs) 20 ---
BOD(ppm) 200 <5
TSS(ppm) 180 <5
NH3(ppm) 20 <0.1
TN (ppm) --- <3
Northern Moraine Utility Commission
Glenbeulah, WI

41. Northern Moraine Utility Commission

42. Northern Moraine Utility
Commission

43. Northern Moraine Utility Commission
 Consistent performance
 Cold wastewater
compatible
 Single digit effluent
 Total nitrogen removal
 Grit removal important

44. MSABPTM
SYSTEM COMPONENTS
 Fine screening & grit removal
 Diffused aeration
 Fixed growth capture media
 Aeration blowers
 Instrumentation

45. SCREENING AND GRIT
REMOVAL
 Pretreatment screening
and grit removal
 Fine screen, 1 mm
openings rotary drum
style.
 Internally fed rotary drum
preferred.
 Standard grit removal for
municipal applications
 Removal of inerts

46. Headworks
 Generate 6-8 ft3
screenings per MG
 30-40% solids
 Relatively stable
 Landfill disposal

47. DIFFUSED AERATION SYSTEM
 Fine pore or coarse
bubble diffused
aeration
 Oxygen provided to
satisfy process
demand in all stages
 Aerated mixing
controls biological
attachment

48. FIXED GROWTH MEDIA
AND FRAMES
 Polyamide & polypropylene
material
 0.25 #media/ft3
of reactor
volume
 Uniform density to support
population
 Support frames are 304
stainless steel
 Integral covers or basin

49. AERATION BLOWERS
 Duty and standby
blower configuration
 Positive
displacement with
sound enclosure

50. INSTRUMENTATION
AND CONTROL
 Instrumentation
– Dissolved Oxygen
– Optical Probes our choice
 Control
– Oxygen in first stage
– Check mid point
– Blower output feedback

51. TYPICAL MUNICIPAL
MSABP Dissolved Oxygen Gradient
0.2
0.6
1
1.5
2
2.7
3.4
4.1
4.6
4.8
4.9 5
Stage
#1
Stage
#2
Stage
#3
Stage
#4
Stage
#5
Stage
#6
Stage
#7
Stage
#8
Stage
#9
Stage
#10
Stage
#11
Stage
#12
MSABP Stages v.s DO
DO, ppm

52. SYSTEM PERFORMANCE
Typical Removal Efficiencies
BOD5 95 – 99%
COD 85 – 95%
TSS 95 – 97%
NH3 90 – 99%

53. PHOSPHORUS REMOVAL
 No Bio-P with MSABPTM
process
 Alum or ferric addition following last stage, 10
min HRT
 Precipitation Stage for 2 hr HRT
 1 mg/l
 Filtration for fractional P

54. TYPICAL PROJECTS
Sharon Labs
Fine Chemistry
Israel
Prosintex
Pharmaceutical
Italy
Teva
Pharmaceuticals
Israel
Veolia
(Lipodan) Oil
Israel
Eisen Lubeo
Food Oil
China
Gadot
Chemicals
Israel
JH Ranch
Municipal
California – USA
Johnson & Johnson
Cosmetics
China
Kibbutz Yavne
Municipal
Israel
Tifico
Textile
Indonesia

55. JH RANCH, ETNA, CA
40,000 GPD
Influent Effluent
pH 6.2-7.5 6.8-7.4
COD(ppm) <1,000 <60
BOD(ppm) <450 <10
TSS(ppm) <250 <10
N-NH3(ppm) <100 <1.0

56. TEVA PHARMACEUTICAL,
ISRAEL 80,000 GPD
Influent Effluent
pH 6.0-9.0 6.0-9.0
COD(ppm) <50,000 <6,000
BOD(ppm) <20,000 <1,000
TSS(ppm) <2,000 <350
TOC(ppm) <15,000 <1,500

57. JOHNSON & JOHNSON, CHINA
13,000 GPD
Influent Effluent
pH 5.6-7.2 5.6-7.2
COD(ppm) <3,000 <300
BOD(ppm) <1,000 <150
FOG(ppm) <30 <10
LAS(ppm) <100 <10
LINEAR ALKYLBENZENE SULFONATE , BIODEGRADABLE SURFACTANT

59. PRETREATMENT

60. GLASS MANUFACTURER
STAGE 1
STAGE 4
STAGE 12

61. O-I GLASS
Influent
Effluent
Influent Effluent
BOD(ppm) <700 <15
TSS(ppm) <300 <40
O&G(ppm) <150 <5

62. PORTABLE TREATMENT UNIT
NORTHERN MORAINE UTILITY

63. STAGES 1, 6 AND 12

64. INFLUENT STAGE 6 EFFLUENT

65. NMUC WWTP Influent Characteristics
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150
160
170
180
190
200
210
220
230
240
250
3/18
3/22
3/25
3/29
4/1
4/5
4/8
4/12
4/15
4/19
Sample Date
Concentration(mg/l)
INF BOD
INF SS
INF NH3
INF TKN
NMUC WWTP Effluent Performance
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
9.0
10.0
11.0
12.0
13.0
14.0
15.0
3/18 3/22 3/25 3/29 4/1 4/5 4/8 4/12 4/15 4/19
Sample Date
Concentration(mg/l)
EFF BOD
EFF SS
EFF TN
EFF TKN
EFF NH3
COLD WEATHER PERFORMANCE

66. STAGE 1 FREE SWIMMER &
BEGGIATOA

67. STAGE 4 - BRISTLEWORM

68. STAGE 6 - GASTROTICH

69. STAGE 10 - ROTIFER

70. WAL-MART SUPER CENTER

71. BEFORE AND AFTER
Influent Effluent
BOD(ppm) 2520 86
TSS(ppm) 1560 200
O&G(ppm) 63 6

72. FINE SCREENING

74. KIBBUTZ KVUZAT YAVNE,
ISRAEL 210,000 GPD
Influent Effluent
pH 6.0-8.0 6.0-9.0
BOD(ppm) <300 <20
TSS(ppm) <100 <30
N-NH3(ppm) <80 <1.0

75. PERFORMANCE PER STAGE
MSABP Kinetic
0
50
100
150
200
250
300
350
400
450
2 4 6 8 10 12 14 16
HRT, hours
Concentration,ppm
BOD
TSS
NH4

76. Yavne WWTP Performance Data
0
100
200
300
400
500
600
700
800
900
1,000
1,100
1,200
7.06.06
15.06.06
21.06.0626.06.06
6.07.06
13.07.06
25.07.06
30.07.06
7.08.06
16.08.06
29.08.06
11.09.06
19.09.06
5.10.06
18.10.06
6.11.06
15.11.06
23.11.06
10.12.06
4.01.07
30.01.0725.02.07
22.03.07
20.06.07
Sample Date
Concentrationppm
Influent COD ppm
Effluent COD ppm
Parameter Average Influent (ppm) Average Effluent (ppm)
COD 538 83

77. Yavne WWTP Performance Data
0
20
40
60
80
100
120
140
160
180
200
220
240
260
280
300
320
340
360
380
400
420
440
460
480
500
520
540
7.06.06
15.06.06
25.06.06
4.07.06
11.07.06
23.07.06
27.07.06
3.08.06
13.08.06
20.08.06
11.09.06
27.09.06
12.10.06
22.10.06
9.11.06
16.11.06
30.11.06
4.01.07
30.01.07
25.02.07
22.03.07
20.06.07
Sample Date
Concentrationppm
Influent TSS ppm
Effluent TSS ppm
Parameter Average Influent (ppm) Average Effluent (ppm)
TSS 186 19

78. Yavne WWTP Performance Data
0
5
10
15
20
25
30
35
40
45
50
55
60
65
70
75
80
85
90
95
7.06.06
13.06.06
21.06.06
28.06.064.07.067.08.068.08.06
13.08.06
16.08.06
17.08.06
20.08.06
29.08.065.09.06
11.09.06
14.09.06
17.09.06
31.10.066.11.069.11.06
12.11.06
15.11.06
16.11.06
19.11.06
23.11.06
30.11.06
10.12.06
25.12.06
31.12.064.01.078.02.07
Sample Date
Concentrationppm
Influent NH3 ppm
Effluent NH3ppm
Parameter Average Influent (ppm) Average Effluent (ppm)
NH3 55 0.69

79. PORT WASHINGTON, WI

80. Influent vs Effluent
Port Washington
MSABP Pilot
0
25
50
75
100
125
150
175
200
225
250
275
300
2/25/09
3/3/09
3/10/09
3/17/09
3/24/09
3/31/09
4/7/09
4/14/09
4/22/09
4/29/09
5/4/09
mg/L
influent ammonia influent BOD influent TSS influent total P effluent ammonia effluent BOD effluent TSS effluent total P

81. TEMPERATURE
Cell #1 water temp
Port Washington MSABP
5.0
6.0
7.0
8.0
9.0
10.0
11.0
12.0
13.0
14.0
15.0
16.0
17.0
18.0
19.0
20.0
21.0
22.0
2/16/092/20/092/26/093/4/093/10/093/16/093/20/093/26/094/1/094/7/094/14/094/20/094/24/094/30/095/6/095/12/095/18/095/22/095/29/096/4/096/10/096/16/096/20/096/25/097/1/097/8/097/14/098/6/098/12/098/19/098/25/099/1/099/8/09
11/16/09
11/20/09
11/30/0912/4/09
12/10/09
12/16/09
12/29/091/8/101/15/101/21/10
Temp(deg.C)
water temp

82. NTU FEBRUARY 2009
NTU
Port Washington
MSABP Pilot Unit
February
0
1
2
3
4
5
6
7
8
9
10
2/15/09
2/16/09
2/17/09
2/18/09
2/19/09
2/20/09
2/21/09
2/22/09
2/23/09
2/24/09
2/25/09
2/26/09
2/27/09
2/28/09
3/1/09
3/2/09
NTU

83. AS A RESULT
 JENNINGS NORTHWEST
REGIONAL UTILITY
SELECTS MSABP.
 UPGRADE FROM CURRENT SBR TECHNOLOGY
 0.35 – 1.7 MGD CAPACITY
 FEBRUARY 2011 STARTUP

89. PLANT EFFLUENT

91. NMUC IN OPERATION

92. NEW HEADWORKS

93. INFLUENT EQ

94. STAGE 1, STAGE 6

95. STAGE 12

96. MSABP SUMMARY
 Fine screening, long HRT, hyper plug flow, selector technology
with discrete spatial zones and attached growth allow the
organisms to function without waste sludge production.
 Operational control is simple and automatic
 Stable
 Cost Effective and Beneficial Process

97. UNDER CONSTRUCTION
 ROUNDUP RIVER RANCH, CO
 WAYNE, NE
 MANCOS, CO
 TORTILLA KING, KS
 DRIGGS, ID

98. Influent Effluent
Flow(gpd) 4,000 ---
HRT(hrs) 12-24 ---
BOD(ppm) 175 <10
TSS(ppm) 200 <10
NH3 (ppm) 30 <1
TN (ppm) 60 <10
Roselle, Illinois - Devlin WWTP

99. Roselle, Illinois
 “…roughly $100,000 annually
to haul its sludge…”
 “…estimated it would save $9
million…”

100. Effluent Turbidity

101. NH3N TN
Influent 28.3 57.2
Stage 2 18.1 36.6
Stage 4 0.346 20.0
Stage 6 0.031 13.2
Stage 8 0.031 9.2
Stage 10 0.027 7.9
Stage 12 0.021 4.3
Nitrogen Balance

102. Influent Effluent
Flow(gpd) 25,000 ---
HRT(hrs) 16 ---
BOD(ppm) 650 <225
TSS(ppm) 650 <225
Wal-Mart, Alpharetta, GA
25,000 GPD Pretreatment Facility

103. Influent Effluent
Flow(gpd) 85,000 ---
HRT(hrs) 24 ---
BOD(ppm
)
300 <25
TSS(ppm) 300 <35
NH3(ppm) 40 <1
TN (ppm) --- <15
Villarrin de Campos - Zamora, Spain
 Retrofit
 Improved performance

104. Villarrin de Campos - Zamora, Spain

105. MSABP Operations
Savings Per MGD
1,900 #/day waste sludge generation
Capital Cost
20 day storage digester (450,000 gal tank @ $600 yd3
concrete) $200,000
Aerobic digester aeration system $50,000
Aerobic digester blower system $75,000
Belt press, polymer feed system $150,000
Building, HVAC, etc. $100,000
Total $575,000
Annually
Mixing power (30 scfm/kcf @ $0.07 / kw-hr) $35,000
Polymer ($12/ ton dry solids) $4,000
WAS disposal (20% conc. @ $37 / wet ton) $65,000
Total $104,000

106. 20 Year Present Worth Savings*
$1,567,100
* 7% discount rate

107. Contact Information
 Contact: Jack Akin, MS, PE
 Cell Phone: 541-474-9434,
Ext. 1
 Email:
bioscapetechnologies@charter.net
 emc@emcengineersscientists.com
 Jacksonville Office Address:
450 Conestoga Drive,
Jacksonville, Oregon, 97530