Agenda Introduction to Cambi What is Thermal Hydrolysis Main - - PowerPoint PPT Presentation

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Agenda Introduction to Cambi What is Thermal Hydrolysis Main - - PowerPoint PPT Presentation

Agenda Introduction to Cambi What is Thermal Hydrolysis Main Benefits Cambi THP Plant Configuration DC Water Blue Plains Project THP O&M Cambi the Company Started late 1980s in Norway as Kambi


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SLIDE 1
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SLIDE 2

Agenda

  • Introduction to Cambi
  • What is Thermal Hydrolysis
  • Main Benefits
  • Cambi THP Plant Configuration
  • DC Water Blue Plains Project
  • THP O&M
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SLIDE 3

Cambi the Company

  • Started late 1980’s in

Norway as Kambi

  • Technology originally

developed for the paper pulping industry

  • Company bought by Petrol

Holdings in early 1990’s

  • Odd Egil Solheim & Per

Lillebø

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SLIDE 4

Cambi the Company

Cambio = change (Spanish masculine noun) Currently

  • 150 Employees
  • Offices in China, USA, UK,

Germany, Spain, Singapore and headquartered in Asker, Norway

  • Manufacturing facility in

Manchester, UK

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SLIDE 5

Cambi THP Systems Worldwide

  • 1995 - First full scale facility in

Hias, Norway

  • Over 55 Installations or

contracts worldwide

  • 20 Years of continuous
  • peration
  • 2015 - First operational

installation in United States - the BIGGEST IN THE WORLD!

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SLIDE 6

Worldwide Capacity

200 400 600 800 1,000 1,200 1,400 1,600 1996 1997 1998 1999 2000 2001 2002 2003 2004 2005 2006 2007 2008 2009 2010 2011 2012 2013 2014 2015 2016 2017 Thousands tonnes dry solids/year (capacity) New Capacity Online, DTPY Cumulative Capacity, DTPY

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SLIDE 7

CAMBI SERVES A POPULATION OF MORE THAN

50 MILLION PEOPLE WORLDWIDE

SEOUL – DUBLIN – OSLO – BRUSSELS – ATHENS SANTIAGO DE CHILE – EDINBURGH – CARDIFF – AND 20+ OTHER CITIES BEIJING LONDON WASHINGTON DC SINGAPORE

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SLIDE 8

What is Cambi Thermal Hydrolysis?

Process for preconditioning biosolids prior to anaerobic digestion Stage 1: Pressure Cooker

  • Dissolves extra-cellular

polymetric substances (EPS)

  • Increases solubility
  • Time/temperature destroys

pathogens resulting in Class A Biosolids

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SLIDE 9

Stage 2: Rapid Depressurization

Rapid depressurization results in steam explosion, cellular disintegration and a dramatic decrease in viscosity

Cells Before Hydrolysis Cells After Hydrolysis

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SLIDE 10

Dramatic Viscosity Reduction

Dewatered Cake 16.5%tds Hydrolyzed Sludge 14%tds Digester Feed 10.5%tds Digested Sludge 5 - 6%tds Dewatered Cake 30 - 35%tds

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SLIDE 11

Thermal Hydrolysis Main Benefits

  • Highly digestable solids
  • Accelerates Volatile Solids Reduction (VSR) and methane

production

  • Lowers required Digester Hydraulic Retention Time (HRT)
  • Increase in high quality methane gas production
  • Maximizes use of existing

infrastructure

  • Reduces or elimininates

the need for expansion

  • Great end produce
  • Class A, highly dewaterable

end product

  • Lower quantity for disposal

= cost savings

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SLIDE 12

Thermal Hydrolysis Plant Configuration

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SLIDE 13

Cambi THP Animation

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SLIDE 14

DC Water Blue Plains - THP

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SLIDE 15

Blue Plains Overview

  • 391 mgd average day

capacity

  • ~160 acres
  • Serves DC, plus

areas of MD and VA

  • Advanced secondary

treatment – filtration, N and P removal

  • Discharges to

Potomac River and Chesapeake Bay

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SLIDE 16

Planning and Research Spanned 10 Years

00-HHE-ST 01-CTS-01 03-CTS-9T 04-CTS-3T SRSK4T08 - Ongoing

Quality Research Technology Research

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SLIDE 17

Class B Bio Solids Land Application

1200 wet tons/day of lime stabilized biosolids

  • Agriculture – 39 counties in MD and VA
  • Silviculture – 40,000 acres permitted in 8 Virginia counties
  • Poplar plantation on a gravel mine
  • Reclamation projects – three sites to date
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SLIDE 18

Project Drivers and Objectives

1. Biosolids planning goals

  • Produce Class A Biosolids
  • Reduce final quantity
  • Enhance long term reliability
  • 2. Generate electricity to

meet one third of Blue Plains needs 3. Reduce project costs

  • Higher loaded, smaller

digesters

  • Smaller project footprint

Main Process Train (MPT) Aerial Rendering

Digesters Screening THP Pre-Dewatering CHP

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SLIDE 19

THP Project Design & Delivery

  • Four independent Cambi THP

trains each rated at 112.5dtpd. Whole system rated at 450dtpd.

  • Design based on standard B12

linear train layout with six reactors per train.

  • Manufactured in the US and UK.
  • 20 month site installation started

August 2012.

  • Control system by Emerson –

Ovation PCS.

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SLIDE 20

THP Overview – Emerson PCS

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SLIDE 21

Feed Loop Overview – Emerson PCS

  • TH solids fed at 10.5%tds to four 3.8 million gallon digesters
  • Increased feeding flexibility of the loop design
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SLIDE 22

THP Commissioning & Start-up Commissioning

  • Thorough control system

testwork with Emerson carried

  • ut both off and on site.
  • Systems integration, including

surrounding support systems.

  • THP trains functionally tested

using water.

  • Full Automatic operation with

water.

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SLIDE 23

THP Pressure Trends

  • Heat and pressure are generated via steam from CHP facility.
  • Approx. 1 pound of steam per pound of solids is required.
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SLIDE 24

THP Commissioning & Start-up

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SLIDE 25

THP Commissioning & Start-up Plant Start-up

  • A very cautious approach was

taken, one train operating intermittently feeding approx. 20,000lbs of VS into digester 1 on day 1 (around 7% of the existing VS in the digester)

  • THP throughout ramped up 3-5%

each day.

  • All THP trains started up over the

following three months.

  • Processing all of DC Water’s

sludge by March 2015.

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SLIDE 26

The “Intensified Cambi Digester”

5 10 15 20 25 30 35 40 45 50 20 40 60 80 100 120 140

Hydraulic Retention Time (days) Feed Rate - Tons Dry Solids per Day at 10.5%TDS

DC Water Digester Loadings Digester #1 of 4

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SLIDE 27

Project Summary

Process Performance

Operational targets:

  • Cambi feed sludge TS – 16.5%
  • Digester feed TS – 10.5%
  • Cambi reactor – 87 psi, 330oF

Digester conditions:

  • Temperature = 100oF
  • TS = 5.5 %
  • Ammonia-N = 2800 mg/L
  • pH = 7.6
  • Bicarbonate alk = 8,000 mg/L +/-
  • Approx. 65% VSR

Reached Class A February 2015

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SLIDE 28

Project Summary

Beltpress Performance

  • Loading rate:
  • 1000 lbs/m/hr avg
  • 1500 lbs/m/hr peak
  • Diluting feed from 5% to 3.5%
  • Cake TS = 30 - 32%
  • Polymer dose = 18 lb/dt +/-
  • Filtrate and wash water are

collected separately

  • High ammonia filtrate will be

treated using DEMON (2017)

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SLIDE 29

Project Summary

Cambi THP O&M

Training:

  • O&M Training complete May 2015
  • Shadow Training complete July 2015

DC Water Operations:

  • Two operators for whole MPT due to

fully automated operation

  • Operators monitor, sample and carry
  • ut daily PM’s

DC Water Maintenance:

  • Carry out more major PM’s –

averages around two hours per week for THP

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SLIDE 30

Modular Cambi THP

B-2 System: 8 x 40’ Footprint 24 dry tons per day B-6 System: 30 x 40’ Footprint 90 dry tons per day

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SLIDE 31

Thank you

Benn Astbury benn.astbury@cambi.com