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448 19 Perspectives of Wastewater, Waste, Off-gas and Soil Treatment

tions an indigenous microbial population exists and that degradation has already occurred and is continuing. To support or enhance this natural self-curing ability, bioaugmentation and biostimulation technologies are available and sometimes suitable. In all situations, degradation rates, degradation efficiency, and groundwater flow rates should be carefully monitored, and the remediation area should be planned far enough downstream in the groundwater to avoid transportation of contaminants or metabolites out of the remediation field. By construction of funnel- and-gate systems (reactive walls) at the downstream end of the remediation field, nondegraded contaminants and residual metabolites can be adsorbed onto activated carbon or other suitable materials and be prevented from migrating into noncontaminated areas.

19.6

Drinking Water Preparation

If the groundwater contains toxic substances as a consequence of soil pollution by leachates from sanitary landfills, production residues, spillages from industry, overfertilization, or insecticide and pesticide application in agriculture, these substances must be separated quantitatively during water processing for drinking water preparation. Separation, filtration, and sanitizing procedures have been developed and have reached high technological levels. Since contamination of groundwater is still increasing and many contaminants remain for decades, water purification procedures must have high priority now and in the future, especially since drinking water resources are limited.

In arid countries with access to saline seawater, the water must be desalted by membrane-based seawater desalting processes to obtain salt-free process water or drinking water.

Although techniques for complete purification of wastewater are in principle available, the application of these multistep procedures to drinking water preparation is not likely in the near future, because of the very high water processing costs and the availability of less polluted water sources.

19.7

Future Strategies to Reduce Pollution and Conserve a Natural, Healthy Environment

In industrialized countries the main strategy for handling domestic and industrial wastewater seems to be set for years or even decades, due to high investments in sewer systems and in what is considered modern wastewater treatment facilities. High-efficiency removal of carbon, nitrogen, and phosphate was intended in the past as a way to avoid damage to the receiving ecosystems.

In Germany, centralized treatment centers fed with hundreds of miles of sewers and many pumping stations have been almost completed for domestic wastewater treatment. ‘Spot solutions’ for new residential areas, single houses, or small villages

19.7 Future Strategies to Reduce Pollution and Conserve a Natural, Healthy Environment 449

should be promoted to gain experience with the new small-scale process alternatives.

The real challenge for wastewater purification arises in many developing countries lacking sewer systems and often lacking any wastewater treatment. Central treatment units are unaffordable, and even if they existed the sewer systems would not be capable of handling the masses of rainwater during the rainy season. This is why decentralized wastewater and waste treatment should be favored. ‘Decentralized’ in this context should range from single-house solutions, neighborhood solutions for a few houses, wastewater treatment solutions for a residential area or municipality, to solutions for a certain geologically defined area of human settlement. If the whole infrastructure for wastewater collection and treatment must be designed, the best solution would be the one with the shortest overall sewer length. Due to the still-unreliable electric supply outside the megacities, small-scale treatment systems should be reduced to the basic components as a starting technology, requiring little or no electricity and no skilled personnel for maintenance. Decentralized wastewater management should be favored, not only because imitating the systems of industrialized countries would not be affordable, but because the wastewater resources could be better used. Domestic wastewater and wastes, if properly collected and treated, can be upgraded to yield valuable nitrogenand phosphate-rich fertilizers and thus save money otherwise spent on mineral fertilizers. By decentralized treatment, more nontoxic wastewater, sewage sludge, or waste compost as a source of nitrogen and phosphate is available for treating local farmland, and transport distances are short.

A process development that goes hand in hand with investigations on the respective microbiology is very important for the future development of wastewater treatment. Microbial reaction rates are higher in equatorial countries due to the high average annual temperatures.

Future microbial investigations for wastewater treatment should start with the complex ecophysiology and end with tracing and optimizing single microbial bottleneck reactions. As recently experienced with the Anammox (anaerobic ammonia oxidation) process, microbiology often seems to lag behind technical verification. Other new procedures for the removal of nitrogen from domestic or industrial wastewater are at the stage of pilotor technical-scale testing. In parallel, microbiologists are elucidating the biochemical basis of the relevant reactions.

Although in some branches of the food and feed industries, starter cultures or even enzymes are now essential tools for production, the advantage of a broad application of starter cultures to wastewater treatment (bioaugmentation) in order to improve purification efficiencies or to degrade trace compounds is not yet widely recognized. Most reports refer to laboratory-scale experiments; only a few full-scale tests have been reported. Starter cultures containing genetically engineered specialists for metabolizing certain xenobiotics that periodically appear in more than trace concentrations may, however, help to introduce or stabilize the required metabolic capabilities. Starter cultures containing an ‘omnipotent’ population may be seeded only after complete process failure due to the presence of toxins, to reestablish the microbial degradation potential more quickly in wastewater treatment plants receiv-

450 19 Perspectives of Wastewater, Waste, Off-gas and Soil Treatment

ing wastewater having little indigenous population. Biostimulation of the autochthonic population by addition of extra substrates or electron acceptors is an alternative to be considered.

A major problem at present and in the future is the handling of surplus sludge from wastewater treatment. Dewatering procedures must be improved, and new and better sludge disintegration methods must be developed. Although in some examples the microbiological basis for the formation of bulking sludge is understood, reliable microbiological counteractions to prevent bulking are not yet available. For sludge disintegration, enzyme engineering should in the future create new, stable, and powerful lytic enzymes.

For water management in new residential areas, developments might go in the direction of dual water supply, on-spot treatment of slightly polluted wastewater, and seepage of purified wastewater in especially designed ecosystems. Concentrated wastewater streams should also be treated near to where they are generated. New residential areas must be planned with few paved areas (or existing paved areas should be depaved), so as to retain most of the rainwater for replenishing the groundwater.

Industrial production processes with better product-to-wastes ratios have to be developed by applying new production processes or by more efficient utilization of the water, e.g., by internal water cycling. Tailor-made treatment systems for every wastewater stream should be optimized, with emphasis on production procedures and on microbiological capabilities, including the use of starter cultures (bioaugmentation).

The slogan ‘the waste of one company is the raw material of another’ should be promoted worldwide and may be facilitated by creation of appropriate databanks. Retail prices for all goods, including those imported from developing countries, should include the full, real, or fictive costs for wastewater and residue treatment.

The potential to reduce the total amount of solid wastes in the future must be fully exploited, in particular by the packaging industry. Improvement of distribution logistics may help to prevent one-way single-product packaging, pallet-level packing and another layer of packaging for transport of larger package units.

Since incineration is the most expensive waste destruction system, it should be reserved only for those fractions that cannot be recycled or reutilized. Biowaste composting and biowaste methanation are options for organic waste fractions having a high content of naturally occurring organics. Cofermentation of biowaste fractions with sewage sludge may also be taken into consideration, if excess digester volume is available and the sewage sludge is free of toxins. Combined mechanical and biological waste inertization could be an alternative to incineration, but cannot achieve the low carbon content required by the deposition guideline of the EU.

In developing countries, direct reutilization of wastewater or wastes or product recycling seems to be more distributed than in highly industrialized countries, due to a shortage of raw materials or to restricted production or affordability. This is especially true for, e.g., plastic bottles and containers, which are often one-way articles in industrialized countries, but are reutilized several times in developing countries.

In industrialized countries, drinking water management must in the future take care of trace pollutants that have unknown effects on human health. New methods

19.7 Future Strategies to Reduce Pollution and Conserve a Natural, Healthy Environment 451

to analyze and separate residual agricultural and household chemicals and their metabolites must be developed.

Due to the high number of contaminated areas in almost every country and due to limited budgets for soil remediation, such areas should be ranked according to environmental risk. Then soil remediation techniques should be chosen that will prevent further migration of the contaminants or their possibly toxic reaction products. In addition to the common techniques for groundwater treatment (pump-and-treat, funnel-and-gate systems and reactive barriers) increasingly have to be used. For natural attenuation of contaminated areas, gen probe methods must be developed to analyze the biological or biochemical potential in-situ or from in-situ samples. In the U.S. the Environmental Protection Agency requires proof of the degradative capability of the in-situ population.

For treatment of sites with low contaminant concentrations, phytoremediation approaches for metals and organics, e.g., nitro compounds and polycyclic aromatic hydrocarbons, increasingly have to be tested. Together with other near-natural processes and the monitored natural attenuation procedures, sustainable strategies have to be developed to overcome the problems of contaminated sites. Furthermore, a variety of bacterial species and enzymes have been the target of genetic engineering to improve the performance of biodegradation, control degradation processes, and detect chemical pollutants and their bioavailability. Avoidance of environmental contamination is the future challenge for which suitable and sustainable strategies can be achieved only by an interdisciplinary collaboration between all protagonists in research and industry. The wide-ranging experience accumulated with respect to the contamination of soils and groundwater must provide a special impetus for testing the environmental impact of new chemical products before they are introduced, thus preventing subsequent contamination and undesirable reactions, such as the endocrine disruption suspected to be caused by Bisphenyl A. A benign ‘design chemistry’ would, therefore, have to concentrate research on identifying forms of bonding that facilitate the development of biodegradable and environmentally sound chemical products.

The supply of good-quality drinking water must especially be improved in developing countries. to reduce mortality, especially in children. Groundwater pumping from deep wells often exceeds the amount of newly formed groundwater, so wells are drilled deeper and deeper. In coastal regions this may lead to salt water infiltration, which contaminates the sweet water reserves.

Wastewater seepage and groundwater pumping often occur close together, too close to maintain a sufficient purification distance for complete degradation and sufficient sanitization. Contamination of well water with pathogenic microorganisms is favored by this mismanagement and in warm climates causes epidemics.

Off-gas purification by biological means has seen much-increased use in the past. For biological off-gas purification, existing gas ventilation, washing, and filtration techniques and the appropriate technical equipment must be improved further.

453

Subject Index

α-hydroxybutyrate

31

 

 

accumulibacter phosphatis

31

acetate

15

 

 

 

 

 

acetic acid, conversion of 176

acetobacterium woodii

14

 

acetogenic bacteria

12, 14, 15, 20, 21, 357

acinetobacter sp.

 

31, 32

 

activated sludge models

88, 91, 122ff.

–

aeration

122

 

 

 

 

 

– ASM1

 

124, 126

 

 

 

–

ASM2

 

124, 127, 128, 129

– ASM3

 

124, 127

 

 

 

–

COD fractionation

129

 

–

component participation

124

– components

123

 

 

 

–

computer programs

131

 

–

hydraulic patterns

123

 

–

mass balances

 

124

 

 

–

model calibration

130

 

–

phosphorous uptake

127

 

–

process for heterotrophic organisms 127

–

process matrix

 

126

 

 

–

processes 123

 

 

 

 

–

rates

124

 

 

 

 

 

–

transport processes

122

 

–

treatment plant layout

122

–

use of model calculations

131

–

wastewater components

128

activated sludge process

90, 95, 99, 113,

 

115, 101, 115

 

 

 

 

 

–

attached growth material

84, 85

–

bulking

98

 

 

 

 

 

–

carbon removal

101

 

 

–

closed-loop, tanks

99

 

–

denitrification

 

93, 98

 

–

design loads

115

 

 

 

–

development of

79

 

 

–

effluent quality

115

 

 

–

final clarifier

113, 79ff.

 

–

high-rate reactors

85

 

 

–

membrane separation

85

 

 

–

microbiological aspects 86, 90

 

–

mixing tanks

99

 

 

 

 

–

nitrification

90, 93

 

 

 

–

nitrogen removal

101, 113

 

–

phosphorus removal

95

 

 

–

plant configurations

99

 

 

–

process configuration

115

 

–

process description

79

 

 

–

pure oxygen

84

 

 

 

 

–

single-stage process

79, 84

 

–

sludge volume index SVI

98

 

–

technological aspects

86

 

 

additives, use in keep technology 277

 

aeration

80

 

 

 

 

 

 

 

aeration efficiency

101

 

 

 

aeration rate

8

 

 

 

 

 

 

aeration tanks

100

 

 

 

 

aerobic bacteria

205

 

 

 

 

–

predominant bacteria in polluted soils 205

–

principles of bacterial degradation

205

aerobic degradation see also bacterial

 

 

degradation

 

 

 

 

 

 

aerobic degradation

206ff., 236

 

–

alkylphenol

210

 

 

 

 

–

aniline

210

 

 

 

 

 

 

–

aromatic compounds

210

 

 

–

aromatic compounds, degradation

236

–

benzene

210

 

 

 

 

 

–

benzoate

210

 

 

 

 

 

–

biosurfactants

208

 

 

 

–

by cometabolic degradation

212

 

–

by fungi

216

 

 

 

 

 

–by growth

–cooperation anaerobic and aerobic bacteria 214

–

cycloaliphatic compounds

208

–

dioxygenase reaction 206

 

–

m-nitrobenzoate 210

 

–

monooxygenase reactions

206

Environmental Biotechnology. Concepts and Applications. Edited by H.-J. Jördening and J. Winter Copyright © 2005 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim

ISBN: 3-527-30585-8

454

Subject Index

 

 

 

 

 

 

 

 

 

–

p-hydroxybenzoate

210

 

 

 

 

 

 

–

pathways alkane degradation

207

 

–

phenanthrene

 

210

 

 

 

 

 

 

–

phenol

210, 212

 

 

 

 

 

 

–

phthalate

210

 

 

 

 

 

 

 

–

toluene

210

 

 

 

 

 

 

 

 

–

trichloroethane

213

 

 

 

 

 

aerobic wastewater treatment processes,

 

 

modelling of

121ff.

 

 

 

 

 

aliphatic hydrocarbons see also

 

 

 

 

hydrocarbons

 

 

 

 

 

 

 

 

aliphatic hydrocarbons

 

216

 

 

 

–

by fungi

 

216

 

 

 

 

 

 

 

 

aliphatic hydrocarbons, anaerobic

 

 

degradation

231

 

 

 

 

 

 

alkanes, anaerobic degradation of 231

 

alternating nitrification–denitrification

 

 

process (Bio-Denitro)

 

110

 

 

 

amino acids

25

 

 

 

 

 

 

 

ammonia

21, 25, 28–30, 33, 92

 

amounts

68

 

 

 

 

 

 

 

 

amounts and concentrations

69

 

amylases

11, 17

 

 

 

 

 

 

 

anaerobic degradation see also anaerobic

 

 

fermentation

 

 

 

 

 

 

 

 

anaerobic degradation see also bacterial

 

 

degradation

 

 

 

 

 

 

 

 

anaerobic degradation

 

4, 7, 229ff.

 

–

aniline

238

 

 

 

 

 

 

 

 

–

aromatic compounds

 

236

 

 

 

–

aromatic hydrocarbons

245

 

 

–

benzoyol-CoA pathway

237

 

 

–

catechol

 

241

 

 

 

 

 

 

 

 

–

comparison to aerobic degradation 229

 

–

cresols

240

 

 

 

 

 

 

 

 

–

degradation of nitroorganics

248

 

–

degradation of sulfonates

248

 

–

ethylbenzene

 

246

 

 

 

 

 

 

–

halogenated organics

 

247

 

 

 

–

hydroquinone

 

241

 

 

 

 

 

 

–

hydroxybenzoates

238

 

 

 

–

hydroxyhydroquinone

244

 

 

–

ketones

235

 

 

 

 

 

 

 

 

–

methanogenic degradation

 

4

 

–

n-alkyl compounds

 

234

 

 

 

–

nitrilotriacetate

234

 

 

 

 

 

–

nonionic surfactants

232

 

 

 

–

of acetone

235

 

 

 

 

 

 

–

of ether compounds

 

232

 

 

 

–

of organic compounds

229

 

 

–

phenol

238

 

 

 

 

 

 

 

 

–

resorcinol

241

 

 

 

 

 

 

–

S-alkyl compounds

 

235

 

 

 

–

toluene

246

 

 

 

 

 

 

 

–

trihydroxybenzenes

242

–

trihydroxybenzoates

242

anaerobic degradation of methane 231 anaerobic fermentation see also anaerobic

 

degradation

 

anaerobic fermentation

355ff.

–

acetic acidand hydrogen-forming

 

(acetogenic) bacteria

357

–

agitation

368

 

–

biochemical fundamentals 356

–

biowaste

364

 

–

biowaste fermentation

363

–

comparison with composting 360

–

composition of biogas

360

–continuous and discontinuous operation 367

–

dry and wet fermentation

366

–

dry or wet fermentation

365

–

garbage waste 355

 

–

gas quantity and composition 359

–

hydrolytic and acid-forming (fermentative)

 

bacteria 357

 

–

inhibitory factors 359

 

–methane-forming (methanogenic) bacteria 357

–

one-stage

365

 

–

oxygen 358

 

– pH 358

 

 

–

process classification

370

–

process engineering

365

–

processes

361

 

–

redox potential 358

 

–

temperature 358

 

–thermophilic and mesophilic operation 368

–

two-stage

365

 

–

water content

358

 

anaerobic glucose degradation

6

anaerobic reactors 4

 

anaerobic wastewater treatment

135f.

– CSTR

136

 

 

–

fluidized bed

136

 

–

high-rate

135, 136

 

–

tapered bed

136

 

– UASB

136

 

 

Anammox®

29

 

aniline, anaerobic degradation of 238 anoxic volume fraction 95

aromatic compounds 210, 211, 217

–

aerobic degradation of

210

–

cometabolic degradation of 217

–

meta cleavage

212

 

–

ortho cleavage

212

 

–

oxygenolytic cleavage

211

aromatic compounds see also Benzene, Toluene, Ethylbenzene, Xylene (BTEX)

aromatic hydrocarbons, anaerobic degradation of 245

Arthrobacter

26

ascorbate 39

ATF process

369

b

 

â-oxidation

3

bacterial degradation see also aerobic degradation, anaerobic degradation

bacterial degradation 214, 229, 231, 232, 234, 245

– alkanes

– aromatic hydrocarbons 245

–cooperation anaerobic and aerobic bacteria 214

–

n-alkyl compounds

234

–

nitrilotriacetate 234

 

–

nonionic surfactants

232

–

of ether compounds

232

–

or organic compounds

–

polychlorinated biphenyls (PCBs) 214

bacteroides 9

 

baker’s yeast production, wastewater of 176

–

equilibrium constants

176

 

basic steps

340

 

 

 

 

 

–

composting technologies

340

 

Basidiomycetes

220

 

 

 

 

–

lignin degradation

220

 

 

benzoate, anaerobic degradation

237

benzoic acid

36

 

 

 

 

 

benzoyl-CoA pathway in anaerobic

 

 

degradation 237

 

 

 

 

bioaugmentation

39f.

 

 

 

biofilm reactors

37

 

 

 

 

biofilms

40, 138ff.

 

 

 

 

–

bacterial adhesion

139

 

 

 

–

characteristics

139

 

 

 

–

concentration profiles

140

 

–

external mass transfer

140

 

–

formation

138f.

 

 

 

 

–

internal mass transfer

141

 

–

kinetics and mass transfer

139

–

support characteristics

142, 143

biofilms, concentration gradients

419

–

diffusion

419

 

 

 

 

 

–

Henry constants

419

 

 

 

biofilters

409, 410, 413, 414, 417, 423,

 

433ff.

 

 

 

 

 

 

 

–

compost

429

 

 

 

 

 

–

elimination capacity (EC)

414

 

–

elimination capacity of biofilter

423

 

 

Subject Index

455

–

empty bed contact time

413

 

 

 

 

–

for controlling styrene emissions

437

 

–

for gasoline vapor 435

 

 

 

–

for odor control at a wastewater treatment

 

facility 435

 

 

 

–

for odors from a livestock facility

433

 

–

for VOC emissions from an optical lens

 

manufacturer 436

 

 

 

–

for wastewater plant odor control

434

 

–

mass loading rate (Bv)

414

 

 

–

removal efficiency (RE)

414

 

 

–

schematic represetation

430

 

 

–schematic view of microbial degradation 417

–

surface loading rate (BA )

413

–

technology 410

 

–

volumetric loading rate (vs)

414

biogas 8, 12, 23

 

biogas reactor see also fixed bed reactor, biogas

 

tower reactor, fluidized bed reactors

biogas reactor

163ff.

 

 

–

axial dispersion coefficient

185

–

circulation velocity

185

 

–

dissociation of CO2

175

 

–

dissociation of H2S

175

 

–

distribution of biomass

188, 190

–

effect of gas recirculation

193

–

gas bubbles, diameter

198

–

gas holdup

186

 

 

 

–

hydrogen sulfide

167

 

 

–influence of hydrostatic pressure biogas production 197

–

kinetics 170

 

–

mass transport 192

 

–

from liquid to the gas phase 192

–

mathematical model

163

–

mathematical modeling 190

–

measuring techniques

167

–

online measurements

167

–online monitoring of organic substances 169

–

pathway of anaerobic biodegradation

172

–

retention of biomass 188

 

–

silicon membrane probe

168

 

–

silicon membrane probe

170

 

–

superficial gas velocity

186

 

–

whey, anaerobic degradation 172

 

biogas tower reactor (BTR)

164, 165, 181,

 

182, 193

 

 

 

–

effect of gas recirculation 193

 

–

elements of a mathematical model

164

–

hydrodynamic

181

 

 

–

laboratory scale

165

 

 

–

liquid mixing behavior

181, 182

 

456

Subject Index

 

 

 

–

models 182

 

 

 

 

 

 

–

pilot scale 165

 

 

 

–

scale-up strategy

165

 

–

technical scale

165

 

 

bioleaching, of metals

326

 

biological degradation

2

biological or chemical phosphate removal 8

biomethanation process

15

 

biopile process 269

 

 

–

biological ex situ processes

269

biopolymer degradation

3

 

biopolymers

8, 15f.,

 

 

–

hydrolysis

8f.

 

 

 

bioreactor process

269

 

 

–

biological ex situ processes

 

bioreactors

287ff.

 

 

 

–

characteristics

288

 

 

–

comparison of

305

 

 

–

diffusion of contaminants

291

–

distriution of contaminants

288

–

dual injected turbulent separation reactor

 

(DITS) 294

 

 

 

–interconnected bioreactors (ISB cascade) 299

– reactor configurations 289

–slurry decontamination process (SDP) 294

bioremediation see also soil remediation

bioscreen

322

 

 

 

 

bioscrubber

 

411, 413, 414

 

 

–

elimination capacity (EC)

414

–

empty bed contact time

413

 

–

mass loading rate (Bv)

414

 

–

removal efficiency (RE)

414

 

–

surface loading rate (BA )

413

–

volumetric loading rate (vs)

414

bioslurping

320

 

 

 

 

biosparging

 

320

 

 

 

 

–

process scheme

321

 

 

 

biosurfactants

208

 

 

 

 

biotrickling filters

410, 413, 414, 432

–

elimination capacity (EC)

414

–

empty bed contact time

413

 

–

mass loading rate (Bv)

414

 

–

removal efficiency (RE)

414

 

–

surface loading rate (BA )

413

–

technology

410

 

 

 

 

–

volumetric loading rate (vs)

414

bioventing

317, 318

 

 

 

–

aromatic hydrocarbons

318

 

–

process scheme

318

 

 

 

biowaste 363ff.

 

 

 

 

–

anaerobic fermentation

364

 

–

delivery and storage

363

 

–

post-processing

 

365

 

 

 

–

preprocessing

364

 

 

 

–

process engineering

365

 

biowaste fermentation

363

 

–

anaerobic fermentation

363

 

–

treatment steps

 

363

 

 

 

brewery wastewater

72

 

 

 

–

amounts and concentrations 72

 

Brocardia anammoxidans

29

 

BTA process

369

 

 

 

 

 

BTEX aromatics

282

 

 

 

–

heap technique

 

279

 

 

 

Buswell equation

23

 

 

 

c

 

 

 

 

 

 

 

 

calibration

170

 

 

 

 

 

Calvin cycle 26

 

 

 

 

 

CANON process

30

 

 

 

carbohydrates

16, 23

 

 

 

carbon removal 87, 88, 101

 

–

Food/microorganism ratio (F/M ratio) 87

–

mixed substances

87

 

 

–

single substancs

87

 

 

 

Cellulomonas

9

 

 

 

 

 

cellulose

16, 9

 

 

 

 

 

–

hydrolysis

9f.

 

 

 

 

 

chlorinated xenobiotics

214

 

chloroaromatics, dehalogenation reactions

 

214

 

 

 

 

 

 

 

citric acid

39

 

 

 

 

 

 

Clavibacter sp.

40

 

 

 

 

Clostridia

14, 20

 

 

 

 

 

Clostridium sp.

6, 9, 14

 

 

 

Clostridium thermoaceticum

14

 

Clostridium thermocellum

 

10

 

compost biofilter

433, 434

 

–

for odors from a livestock facility

433

–

for wastewater plant odor control

434

compost heap, microbial activity in

336

–aerobic conversions 336

–anaerobic conversions 336 compost quality 349

composting

333ff.

 

–

C/N ratio

338

 

 

–

characteristic temperature

339

–

compost quality

349

 

–

composting plant, flow sheet of 350

–

composting technologies

340

–

fundamentals

335

 

–

heavy metal content 335

 

–metabolism of aerobic microorganisms 337

–

nutrient content 334

–

optimal water content 337

–

systems

342

 

 

 

 

 

 

 

–

waste materials for

334, 335

 

 

composting plant, flow sheet of

350

 

composting process

 

338f.

 

 

 

 

–

characteristic temperature

339

 

–

factors influencing

338

 

 

 

 

–

mature phase

339

 

 

 

 

 

–

postcomposting

339

 

 

 

 

–

preand main composting

339

 

composting systems

342, 346ff.

 

 

–

classification

342

 

 

 

 

 

–

nonreactor composting

342

 

 

–

reactor composting

346

 

 

 

–

reactor composting

347

 

 

 

–

reactor composting

348

 

 

 

–

reactor composting

349

 

 

 

composting technologies

340

 

 

–

flow sheet

340

 

 

 

 

 

 

concentrations

68

 

 

 

 

 

 

concentrations of pollutants

59, 62

 

contact stabilization process

81

 

 

contaminants 312

 

 

 

 

 

 

–

degradation limiting factors

312

 

contaminated soil

259ff., 275, 277, 315

–

addition of additives 277

 

 

 

–

biological ex situ process scheme

268,

 

269

 

 

 

 

 

 

 

 

–

biological ex situ processes

269, 270

–

biological in situ processes

270

 

–

biological processes, application of

270,

 

271

 

 

 

 

 

 

 

 

–

bioremediation of

275

 

 

 

 

–

chemical/physical in situ processes

266,

 

267, 268

 

 

 

 

 

 

 

 

–

chemical/physical prococess 265

 

–

disposal

271

 

 

 

 

 

 

 

–

elimination of limiting factors

315

–optimization of biological degradation 315

–soil vapor extraction (SVE)

–the chemical/physical scheme ex situ

 

process 265, 266

 

–

thermal ex situ processes

260, 263

–

thermal in situ processes

263

–

thermal processes 260

 

–thermal processes, A, 264

–treatment

– utilization of decontaminated Soil

271

contaminated solids

287ff.

 

controlled reduction

391

 

–

aeration methods

391

 

–

humidification and irrigation 391

 

cooling water, in industrial wastewater

51

– amounts 51

 

 

 

 

 

 

 

 

 

 

 

 

 

Subject Index

457

cresols, anaerobic degradation of

240

 

 

CSTR

136

 

 

 

 

 

 

 

 

 

cyclic aeration

100

 

 

 

 

 

 

 

cyclohexane, bacterial degradation of 208

cytechol, anaerobic degradatin of

241

 

d

 

 

 

 

 

 

 

 

 

 

 

 

DBA-Wabio process

 

369

 

 

 

 

deamination

3

 

 

 

 

 

 

 

 

dechlorination

37

 

 

 

 

 

 

 

degradation

236

 

 

 

 

 

 

 

degradation of sulfonates

248

 

 

 

–

anaerobic degradation

 

248

 

 

 

dehalogenation, principles of

215

 

Dehalospirillum multivorans

40

 

 

denitrification

2, 8, 27, 28, 94, 95, 93

 

–

anoxic volume fraction

95

 

 

 

–

COD/TKN ratio

94, 95

 

 

 

 

Desulfomonile tiedjei

 

40

 

 

 

 

 

dissociation of CO2 175

 

 

 

 

 

dissociation of H2S 175

 

 

 

 

 

distillery wastewater

73

 

 

 

 

 

–

amounts and concentrations

74

 

DMT–biodyn process

296

 

 

 

–

process configuration

296

 

 

 

Dranco process

369

 

 

 

 

 

 

dry and wet fermentation

366

 

 

 

dual injected turbulent separation reactor

 

(DITS)

300

 

 

 

 

 

 

 

 

–

technical schema

 

 

 

 

 

 

 

dumps, environmental impacts of

399

 

e

 

 

 

 

 

 

 

 

 

 

 

 

effect of gas recirculation 193

 

 

 

effect on activated sludge process

96

 

–

alkalinity and pH

 

96

 

 

 

 

 

–

dissolved oxygen

 

96

 

 

 

 

 

elements of a mathematical model 164

endoglucanases

10

 

 

 

 

 

 

energy dissipation

4

 

 

 

 

 

equilibrium constants 176

 

 

 

 

Escherichia coli

35

 

 

 

 

 

 

 

ethanol

21

 

 

 

 

 

 

 

 

 

ethylenediaminetetraacetate 234

 

 

Eubacterium sp.

6, 14

 

 

 

 

 

expanded granular sludge beds (EGSB) 150

explosives (TNT, RDX)

282

 

 

 

–

heap technique

279

 

 

 

 

 

f

 

 

 

 

 

 

 

 

 

 

 

 

fats

20, 23

 

 

 

 

 

 

 

 

 

fermentative bacteria

21, 357

 

 

 

Fibrobacter

9, 10

 

 

 

 

 

 

 

final clarifier

113

 

 

 

 

 

 

 

458 Subject Index

fixed bed reactor see also stationary fixed-film

 

reactor, biogas reactors

fixed bed reactors

151, 154–156

–

industrial

 

–

laboratory 155, 156

–

operation results

155, 156

–

reactor geometry

151

–

reactor operation

154, 155

–

technological aspects

151

Flavobacterium 26

 

 

 

fluidized bed reactors

135, 144, 145, 152–154

–

anaerobic

137

 

 

 

 

–

bed height

153

 

 

 

 

–

flow distribution system

153

–

fluidization of the support

153

–

laboratory

157

 

 

 

 

–

loss of support

153

 

 

–

operational results

157

 

–

Pilot scale

157

 

 

 

 

–

reactor design parameters

145

–

reactor geometry

152, 157

–

reactor operations

154

 

–

Richardson and Zaki

144

–

technical scale

157

 

 

–

technological aspects

152

food/microorganism ratio (F/M ratio) 87

formate 13

 

 

 

 

 

FORTEC process

297

 

 

fruit juice and beverage wastewater 70

fungi 217, 220, 224

 

 

 

–

basidiomycetes

220

 

 

–cometabolic degradation of aromatic compounds 217

–

degradation of organopollutants

224

funnel-and-gate

324, 325

 

 

–

process scheme 325

 

 

 

g

 

 

 

 

 

 

 

garbage waste fractions

355

 

 

–

semidry anaerbic fermentation

355

–

wet, anaerobic fermentation

355

gas collecting devices 181

 

 

 

gas purification

22

 

 

 

 

genetically modified bacteria

39

 

Geobacteriaceae

34

 

 

 

 

gluconic acid 39

 

 

 

 

glycogen

32, 33

 

 

 

 

 

glycolysis

3ff.

 

 

 

 

 

glycosyl hydrolases

10

 

 

 

h

 

 

 

 

 

 

 

halogenated organics

247

 

 

–

anaerobic degradation

247

 

 

heap technique

275ff.

 

 

 

–

addition of additives

277

–

bioremediation of

275

 

–

BTEX aromatics

282

 

–

explosives (TNT, RDX)

282

–

oxygen supply

281

 

 

–

petroleum hydrocarbons

282

–

phenols 282

 

 

 

–polycyclic aromatic hydrocarbons (PAH) 282

–

principles

276

 

 

 

 

 

 

–

soil extraction

283

 

 

 

 

–

technical solutions

279

 

 

 

–

time course TNT degradatio

284

 

 

heavy metal

24

 

 

 

 

 

 

heavy metal bioavailability 23

 

 

 

heavy metal ions

33f.

 

 

 

 

Henry constant of pollutants

417

 

 

heterocyclic compounds

25

 

 

 

hexoses

12

 

 

 

 

 

 

 

Highbie’s penetration theory 198

 

 

Huber process

297

 

 

 

 

 

hydraulic circuits

319

 

 

 

 

hydrazine

 

29

 

 

 

 

 

 

 

hydrocarbon uptake, role of biosurfactants

 

 

208

 

 

 

 

 

 

 

 

 

hydrocarbon, aerobic degradation of

204

 

hydrogen

14

 

 

 

 

 

 

 

hydrogen sulfide 167

 

 

 

 

 

hydrolysis

 

3

 

 

 

 

 

 

 

hydroquinone, anaerobic degradation of

241

hydroxybenzoates, anaerobic degradation of

 

238

 

 

 

 

 

 

 

 

 

hydroxylamine

28, 29

 

 

 

 

i

 

 

 

 

 

 

 

 

 

 

in-situ remediation 311ff.

 

 

 

–

activated zones, process scheme 322

 

–

benchtop scale

316

 

 

 

 

–

bioscreen

322

 

 

 

 

 

 

–

bioslurping

320

 

 

 

 

 

–

biosparging

320

 

 

 

 

 

–

bioventing

317

 

 

 

 

 

–

evolving technologies

326

 

 

 

–

funnel-and-gate 324

 

 

 

 

–

hydraulic circuits

319

 

 

 

–

hydrogen-release compounds (HRC®)

323

–

indigenous microflora

316

 

 

 

–

metals, treatment of

326

 

 

 

–

monitoring

328

 

 

 

 

 

–

natural attenuation

324

 

 

 

–

oxygen release compounds (ORC®)

323

–

oxygen supply

314

 

 

 

 

–

parameters

316

 

 

 

 

 

–

passive technologies

322