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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