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  • ;1. Case study or Built example
    871 B (108 words) - 15:54, 13 February 2013

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  • {|border="1" style="text-align:center"
    6 KB (782 words) - 11:38, 27 March 2017
  • '''1. OBJECTIVE'''
    1 KB (162 words) - 11:55, 18 January 2013
  • '''1. OBJECTIVE''' A major division may be made between (1)driers in which the solid is directly exposed to a hot gas (usually air) an
    4 KB (668 words) - 11:56, 18 January 2013
  • '''1. OBJECTIVE'''
    1 KB (143 words) - 10:56, 28 March 2017
  • '''1. OBJECTIVE'''
    834 B (124 words) - 10:58, 28 March 2017
  • '''1. OBJECTIVE'''
    979 B (138 words) - 10:58, 28 March 2017
  • '''1. OBJECTIVE'''
    1 KB (147 words) - 10:59, 28 March 2017
  • '''1. OBJECTIVE'''
    2 KB (259 words) - 10:59, 28 March 2017
  • '''1. OBJECTIVE'''
    1 KB (208 words) - 10:59, 28 March 2017
  • '''1. OBJECTIVE'''
    5 KB (753 words) - 10:59, 28 March 2017
  • '''1. OBJECTIVE'''
    850 B (117 words) - 11:01, 28 March 2017
  • '''1. OBJECTIVE'''
    804 B (106 words) - 11:01, 28 March 2017
  • '''1. OBJECTIVE'''
    707 B (91 words) - 11:01, 28 March 2017
  • {| border="1" style="text-align:center" | rowspan="1" style="background:#EECC22"| '''SPINNING'''||[[Spinning in textile industr
    6 KB (668 words) - 13:07, 23 August 2017
  • {| border="1" style="text-align:center"
    8 KB (1,006 words) - 11:37, 27 March 2017
  • {| border="1" style="text-align:center"
    5 KB (483 words) - 11:36, 27 March 2017
  • {| border="1"
    1 KB (116 words) - 08:49, 1 September 2016
  • '''1. OBJECTIVE''' ...ng in the food industry can be divided into three different sub-processes: 1)cleaning of bottles and cases, 2)washing products and 3)cleaning of product
    2 KB (359 words) - 12:35, 21 November 2012
  • <br/>'''1. OBJECTIVE''' ...oisture extraction rate, i.e. kg water removed/kWh energy used, is between 1-4, with an average of 2.5kg/kWh.
    22 KB (3,536 words) - 13:20, 15 October 2013
  • <br/>'''1. OBJECTIVE'''
    2 KB (318 words) - 16:45, 15 October 2013
  • '''1. OBJECTIVE''' ...l chambers. The residence time in the blancher can vary from approximately 1 minute to minutes depending on the vegetable or fruit being blanched.
    5 KB (757 words) - 18:13, 15 October 2013
  • '''1. OBJECTIVE''' Figure 1: Injection and infusion for direct heating in UHT treatment
    9 KB (1,440 words) - 12:37, 21 November 2012
  • '''1. OBJECTIVE''' ...water at boiling temperature. In beer production, wort is boiled for about 1.5 hours in the wort kettle with hops or hop extracts, releasing bitter subs
    4 KB (632 words) - 12:37, 21 November 2012
  • '''1. OBJECTIVE'''
    2 KB (367 words) - 12:37, 21 November 2012
  • '''1. OBJECTIVE'''
    1 KB (213 words) - 12:38, 21 November 2012
  • '''1. OBJECTIVE'''
    2 KB (303 words) - 12:38, 21 November 2012
  • <br/>'''1. OBJECTIVE''' Figure 1: Typical absorption cooling cycle (LITERATURE: [http://lorien.ncl.ac.uk/min
    5 KB (793 words) - 09:45, 21 October 2013
  • <br/>'''1. OBJECTIVE'''
    3 KB (441 words) - 10:32, 21 October 2013
  • '''1. OBJECTIVE'''
    3 KB (513 words) - 12:39, 21 November 2012
  • '''1. OBJECTIVE''' ...ned undesirable compounds. The oil is mixed under vacuum conditions with 0.1-3% of bleaching earth. This is a clay mineral, such as bentonite or montmor
    2 KB (365 words) - 12:40, 21 November 2012
  • '''1. OBJECTIVE'''
    3 KB (481 words) - 11:13, 1 March 2013
  • '''1. GENERAL INFORMATION''' ;1.1 Description, turnover, growth, employment
    16 KB (2,361 words) - 11:38, 28 March 2017
  • '''1 GENERAL INFORMATION''' ;1.1 Description, turnover, growth, employment
    4 KB (568 words) - 11:20, 18 January 2013
  • '''1 GENERAL INFORMATION''' ...packaging, building and construction (for more information, see Section 1.1). Two further commercial areas of application have emerged since the 1960s:
    19 KB (2,731 words) - 11:47, 18 January 2013
  • '''1. GENERAL INFORMATION''' Figure 1: Structure of Industrial Organic Industry, BREF in the Large Volume Organic
    23 KB (3,242 words) - 11:50, 18 January 2013
  • <br/>'''1. OBJECTIVE''' ...ividual zones of the multistage bottle cleaning process are the following: 1)soak, 2)caustic bath, 3)1st zone of hot water tank, 4)2nd zone of hot water
    7 KB (1,008 words) - 15:45, 29 August 2013
  • '''1. OBJECTIVE'''
    2 KB (372 words) - 12:40, 21 November 2012
  • <br/>'''1. OBJECTIVE''' ::1) reduced use of energy needed to heat up water for cleaning,
    6 KB (954 words) - 09:41, 5 September 2013
  • <br/>'''1. OBJECTIVE''' ...p://www3.interscience.wiley.com/cgi-bin/abstract/109062827/ABSTRACT?CRETRY=1&amp;SRETRY=0])<br/>
    4 KB (595 words) - 16:35, 21 October 2013
  • '''1. OBJECTIVE'''
    3 KB (431 words) - 12:43, 21 November 2012
  • '''1. OBJECTIVE'''
    2 KB (395 words) - 12:43, 21 November 2012
  • '''1. OBJECTIVE'''
    3 KB (442 words) - 12:43, 21 November 2012
  • '''1. OBJECTIVE''' Figure 1: Steam peeling process in an example installation in Finland
    11 KB (1,825 words) - 12:43, 21 November 2012
  • '''1. OBJECTIVE'''
    4 KB (551 words) - 14:31, 6 December 2014
  • <br/>'''1. OBJECTIVE''' ...ch the temperature of a food is reduced and kept in a temperature between -1 to 8°C. The objective of cooling and chilling is to reduce the rate of bio
    12 KB (1,809 words) - 16:09, 1 October 2013
  • <br/>'''1. OBJECTIVE''' Figure 1: Typical absorption cooling cycle (LITERATURE: [http://lorien.ncl.ac.uk/min
    8 KB (1,125 words) - 09:10, 7 October 2013
  • ;1.(a) General Flowsheet of short time pasteurized milk: Figure 1: Short time pasteurized milk process LITERATURE: BAT for Food, Drink and Mi
    4 KB (701 words) - 12:45, 21 November 2012
  • ;1. (a) General Flowsheet of condensed milk products: Figure 1: Flowsheet of processes for condensed products (e.g. UHT condensed milk) an
    6 KB (850 words) - 12:18, 1 February 2013
  • ;1. General Flowsheet:
    2 KB (301 words) - 12:04, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet:
    2 KB (218 words) - 12:06, 20 February 2013
  • ;1. Definition: (Dairy science and Technology, University of Guelph, http://ww Figure 1: Overview of the Buttermaking Process LITERATURE: http://www.foodsci.uoguel
    6 KB (911 words) - 12:07, 20 February 2013
  • ;1. Definition: (Dairy science and Technology, University of Guelph, http://ww Figure 1: Manufacture of cheese LITERATURE: BAT for Food, Drink and Milk Industries,
    8 KB (1,214 words) - 12:08, 20 February 2013
  • ;1. Definition: (Dairy science and Technology, University of Guelph, http://ww Figure 1: Yogurt production LITERATURE: BAT for Food, Drink and Milk Industries, Jun
    4 KB (626 words) - 12:04, 20 February 2013
  • ;1. Definition: (Dairy science and Technology, University of Guelph, http://ww ...o 20-25°C before the addition of the starter culture. Starter is added at 1-2% and the fermentation is allowed to proceed for 16-20 hours, to an acidit
    6 KB (937 words) - 12:10, 20 February 2013
  • ;1. (a) General Flowsheet of fruit and vegetable juice manufacturing: Figure 1: Fruit and vegetable juice manufacturing LITERATURE: BAT for Food, Drink an
    4 KB (619 words) - 12:14, 20 February 2013
  • ;1. (a) General Flowsheet of fruit and vegetable juice manufacturing: Figure 1: Fruit and vegetable processing and preservation LITERATURE: BAT for Food,
    2 KB (294 words) - 12:16, 20 February 2013
  • ;1. (a) General Flowsheet of mashed fruit production: Figure 1: Production of mashed fruit.
    798 B (104 words) - 12:17, 20 February 2013
  • ;1. General Flowsheet of dried fruit production: Figure 1: Fruit and vegetable processing and preservation
    2 KB (236 words) - 12:18, 20 February 2013
  • ;1. General Flowsheet of deep-frozen fruit and vegetable production: (BAT for Figure 1: Deep-frozen fruit and vegetable production. Literature: BAT in Food, Drink
    3 KB (451 words) - 12:18, 20 February 2013
  • ;1. General Flowsheet of marmelade pasteurization: Figure 1: Marmelade pasteurization.
    2 KB (329 words) - 12:19, 20 February 2013
  • ;1. General Flowsheet of soup pasteurization: Figure 1: Soup pasteurization.
    791 B (99 words) - 12:20, 20 February 2013
  • ;1. General Flowsheet of soup pasteurization: Figure 1: Soup pasteurization.
    2 KB (325 words) - 12:22, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of various tomato products manufacture: (BAT for Food, D
    3 KB (435 words) - 12:23, 20 February 2013
  • ;1. General Flowsheet of canned fruit production: Figure 1: Fruit and vegetable processing and preservation LITERATURE: BAT for Food,
    2 KB (228 words) - 12:27, 20 February 2013
  • ;1. General Flowsheet of heat treated vegetable production: Figure 1: Fruit and vegetable processing and preservation LITERATURE: BAT for Food,
    2 KB (232 words) - 12:29, 20 February 2013
  • ;1. General Flowsheet of heat treated vegetable production:
    1 KB (174 words) - 12:30, 20 February 2013
  • ;1. General Flowsheet of sugar production: ::''1) Raw cane sugar production:''
    5 KB (774 words) - 12:53, 20 February 2013
  • ;1. General Flowsheet of sugar syrup production:
    481 B (59 words) - 12:54, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. Definition: (BAT in the Food, Drink and Milk Industries, June 2005)
    6 KB (1,021 words) - 13:00, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of vegetable oil production:
    3 KB (500 words) - 13:02, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of olive oil production:
    2 KB (362 words) - 13:03, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of fish production: (BAT in Slaughterhouses and Animal B
    4 KB (708 words) - 13:03, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of margarine production:
    1 KB (216 words) - 13:04, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of cocoa production:
    3 KB (396 words) - 13:07, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of decaffeinated coffee production:
    5 KB (705 words) - 13:07, 20 February 2013
  • <br/>'''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of instant coffee production
    4 KB (631 words) - 22:40, 5 November 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of maize starch production: (BAT for Food, Drink and Mil
    2 KB (389 words) - 13:09, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of wheat starch production: (BAT for Food, Drink and Mil
    2 KB (373 words) - 13:10, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of potato starch production: (BAT for Food, Drink and Mi
    2 KB (325 words) - 13:10, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of sweeteners production
    2 KB (256 words) - 13:11, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of modified starch production
    1 KB (198 words) - 13:11, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of mashed potato production:
    810 B (105 words) - 13:18, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of granulated potato production:
    826 B (105 words) - 13:19, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of potato chips production:
    2 KB (315 words) - 13:19, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of potato crisps production:
    2 KB (335 words) - 13:20, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of grain mill products
    3 KB (487 words) - 13:20, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of soft drink production:
    2 KB (323 words) - 13:34, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of red wine production:
    5 KB (740 words) - 13:35, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of red wine production:
    3 KB (512 words) - 13:35, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of soft drink production:
    3 KB (456 words) - 13:35, 20 February 2013
  • |1
    3 KB (436 words) - 11:47, 3 February 2015
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of canned meat production (beef muscle in gelatine): (BA
    3 KB (450 words) - 12:10, 1 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of cooked ham production: (BAT in the Food, Drink and Mi
    3 KB (436 words) - 12:11, 1 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of cooked ham production: (BAT in the Food, Drink and Mi
    3 KB (413 words) - 12:11, 1 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of special cooking meat production:
    923 B (121 words) - 12:12, 1 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of sausage production:
    2 KB (273 words) - 12:12, 1 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of the production line:
    3 KB (453 words) - 13:39, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of the production line:
    4 KB (597 words) - 13:40, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of the production line:
    2 KB (362 words) - 13:40, 20 February 2013
  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of the production line:
    3 KB (408 words) - 13:40, 20 February 2013
  • ;1. Case study or Built example Case study
    1 KB (196 words) - 11:16, 1 March 2013
  • ;1. Built example ::b) Steam presses: 1.4 m3/day
    3 KB (388 words) - 11:17, 1 March 2013
  • ;1. Built example ::a) 1 steam generator (13 hp) – Heavy oil
    2 KB (342 words) - 11:17, 1 March 2013
  • ;1. Built example
    2 KB (255 words) - 11:17, 1 March 2013
  • ;1. Built example ::Installed thermal capacity [kW] : 11.1 (15.8 m²)
    2 KB (295 words) - 11:18, 1 March 2013
  • ;1. Built example Estimated annual energy savings of 1,400 GJ 70 tonnes of annual CO2 emissions reduction
    3 KB (365 words) - 11:18, 1 March 2013
  • ;1. Case study or Built example ...f removing residual hydrogen peroxide after bleaching and prior to dyeing [1].
    7 KB (1,120 words) - 11:20, 1 March 2013
  • ;1. Case study or Built example Pic. 1: flowsheet: Kufner, textile finishing of knitware and woven fabric
    5 KB (720 words) - 11:20, 1 March 2013
  • ;1. Case study or Built example Bleaching 1
    5 KB (620 words) - 11:20, 1 March 2013
  • ;1. Case study or Built example ...is estimated to be USD 15,135 (MNT 16,196,400) p.a. The payback period is 1.9 years.
    6 KB (853 words) - 11:21, 1 March 2013
  • :1) Relax drier
    2 KB (224 words) - 11:21, 1 March 2013
  • :1) main drier :Cost = Rs.2000/hr [ Rs.40 = 1 US $]
    2 KB (247 words) - 11:22, 1 March 2013
  • ...om coniferous timber and supplied to the fibre manufacture in sheets about 1 cm thick. The wood contains about 40-50% cellulose that is useable to make
    2 KB (239 words) - 11:30, 1 March 2013
  • ...on of 1,3-propanediol and terephthalic acid. The high cost of synthesis of 1,3-propanediol has for many years prohibited the commercialisation of this f ...n reaction, cyclic oligomers with very low water-solubility can be formed (1-3% on the weight of the fibre [77, EURATEX, 2000]. These oligomers tend to
    6 KB (819 words) - 11:33, 1 March 2013
  • :* [[Case studies 1]]
    396 B (46 words) - 08:43, 6 September 2016
  • ::* Cast iron contains 2% – 4.0% carbon , 1% – 6% silicon , and small amounts of manganese. Contaminants present in p ::* Carbon steel contains between 0.4% and 1.5% carbon, with small amounts of manganese, sulfur, phosphorus, and silicon
    11 KB (1,824 words) - 15:57, 13 February 2013
  • ;1. Built example Table 1: Specifications for the built solar system in the Jörg Schiffer industry
    2 KB (292 words) - 15:56, 13 February 2013
  • ;1. Solar integration
    2 KB (297 words) - 15:56, 13 February 2013
  • ;1. Solar integration ...Wh Total energy demand: 2.200.000 kWh, whereof 480.000 kWh electricity and 1.720.000 kWh gas
    3 KB (380 words) - 15:55, 13 February 2013
  • ;1. Case study or Built example
    871 B (108 words) - 15:54, 13 February 2013
  • :* [[Case studies 1]]
    590 B (71 words) - 16:01, 13 February 2013
  • ...1: Overview of the process route of an integrated steel works - [UK IPR 2/1, 1994] - (a pelletisation plant is not shown, as only one integrated steelw
    2 KB (272 words) - 16:00, 13 February 2013
  • :* [[Case studies 1]]
    598 B (72 words) - 16:05, 13 February 2013
  • :* [[Case studies 1]]
    608 B (71 words) - 16:10, 13 February 2013
  • :* [[Case studies 1]]
    399 B (47 words) - 16:15, 13 February 2013
  • :* [[Case studies 1]]
    961 B (112 words) - 16:19, 13 February 2013
  • :* [[Case studies 1]]
    440 B (51 words) - 16:53, 13 February 2013
  • :* [[Case studies 1]]
    389 B (46 words) - 16:56, 13 February 2013
  • :* [[Case studies 1]]
    393 B (46 words) - 16:58, 13 February 2013
  • :* [[Case studies 1]]
    406 B (48 words) - 17:00, 13 February 2013
  • :* [[Case studies 1]]
    394 B (46 words) - 17:02, 13 February 2013
  • :* [[Case studies 1]]
    818 B (96 words) - 17:06, 13 February 2013
  • ...ained now from hot rolling with the new CSP or ISP process, which can roll 1.2 mm now and maybe 0.7-0.8 mm in the future. * Temperature equalisation in the roller hearth furnace (1 per strand) after the casting and before the rolling to achieve a uniform s
    9 KB (1,391 words) - 16:05, 13 February 2013
  • :* [[Case studies 1]]
    450 B (53 words) - 16:13, 13 February 2013
  • ...e overcome by oscillating rollers. The surface roughness should be between 1.5 and 2.5 μm. The subsequent adhesion of dry or liquid resists depends on ...re to restructure the copper surface to a surface roughness of Rz = 1.6 to 1.9 μm, rather than to remove copper. Following this treatment the surface i
    28 KB (4,149 words) - 11:42, 1 September 2016
  • '''1 Overview''' ...ocyanine dyes. The following figure shows the major chromophores and Table 1 shows the classification of dyes by use or method of application.
    20 KB (3,000 words) - 16:35, 14 February 2013
  • '''1. Solar integration'''
    3 KB (436 words) - 16:35, 14 February 2013
  • :Main Heating Blower = 1 no Exhaust Blower = 1 no :Circumference of the pipe = 1.63m (diameter of the pipe = 0.52m)
    4 KB (531 words) - 16:34, 14 February 2013
  • '''1 Overview''' ...D and comprise the largest percentage of new drugs launched yearly. Figure 1.8 gives some examples, but in reality the variety in the world is enormous.
    28 KB (4,189 words) - 16:55, 14 February 2013
  • ''' 1 Overview''' ...n compounds or groups of compounds have been classified as vitamins (Table 1.4). The worldwide market value for vitamins as a bulk product is estimated
    4 KB (599 words) - 16:55, 14 February 2013
  • '''1 Overview''' ...ant health products according to the type of pest they control, and Figure 1.10 gives some examples of biocides and plant health products derived by che
    13 KB (1,959 words) - 16:59, 14 February 2013
  • '''1 Overview''' ...only synthetic compounds used in flavours besides natural products. Figure 1.14 gives some examples.
    4 KB (563 words) - 17:03, 14 February 2013
  • '''1 Overview''' ...white industrial substrates, such as textiles, papers, or plastics. Figure 1.15 gives some examples.
    8 KB (1,119 words) - 17:07, 14 February 2013
  • '''1 Overview''' ...e manufactured, of which at least 100 are of commercial importance. Figure 1.19 shows some of the most widely used plasticisers.
    4 KB (608 words) - 17:12, 14 February 2013
  • ...ium nitrate, and sodium perchlorate. Explosives are dangerous goods (class 1 ADR) and consequently, due to safety concerns Member States have establishe
    2 KB (228 words) - 17:27, 14 February 2013
  • '''1 General description''' Figure 1: Molecular structure of LDPE
    13 KB (1,920 words) - 17:30, 14 February 2013
  • '''1 General description''' Table 1: Properties of DDPE, Literature: Hirschberg, H. G.: Handbuch Verfahrenstech
    8 KB (1,096 words) - 17:33, 14 February 2013
  • '''1 General description''' Figure 1: Molecular structure of LLDPE
    13 KB (1,891 words) - 17:29, 14 February 2013
  • '''1 General description''' Table 1: Properties of PP, Literature: Hirschberg, H. G.: Handbuch Verfahrenstechni
    8 KB (1,133 words) - 17:31, 14 February 2013
  • '''1 General description''' Figure 1: Flow diagram showing GPPS production
    2 KB (340 words) - 17:42, 14 February 2013
  • '''1 General description''' Figure 1: Molecular structure of high impact polystyrene
    2 KB (348 words) - 17:42, 14 February 2013
  • '''1 General description''' Figure 1: Flow diagram showing EPS production
    5 KB (701 words) - 15:08, 21 August 2017
  • '''1 General description''' Figure 1: Flow diagram of an S-PVC process
    2 KB (326 words) - 17:46, 14 February 2013
  • '''1 General description''' Figure 1: Basic condensation reaction scheme for producing unsaturated polyester res
    3 KB (429 words) - 17:48, 14 February 2013
  • '''1 General description''' Figure 1: Main applications of ESBR
    3 KB (379 words) - 17:50, 14 February 2013
  • '''1 General description''' Table 1: production volume share of the major types of synthetic rubber
    9 KB (1,390 words) - 17:53, 14 February 2013
  • 0 B (0 words) - 17:57, 14 February 2013
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    1 KB (166 words) - 11:03, 30 December 2014
  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
    4 KB (549 words) - 12:25, 21 February 2013
  • '''1. Systematics of SystemConcepts''' ::1. Generic system –SPO X – Water:
    839 B (120 words) - 12:26, 21 February 2013
  • ;1. Case study or built example: As can be seen stream 1 in figure above, stream 4 in table xxx needs additional heating. This heati
    3 KB (394 words) - 18:09, 28 November 2014
  • ;1. Solar integration ...d to any process. Of this value, the basic demand requires 4.800 MWh/a and 1.100 MWh/a have to be used for balance-adjustment in the process.
    5 KB (765 words) - 11:57, 20 February 2013
  • ;1. Built example Table 1: Temperature ranges of the process medium and other parameters in the Alpin
    3 KB (418 words) - 11:57, 20 February 2013
  • ;1. Built example Table 1: Temperature ranges of the process medium and other parameters in the Mevga
    4 KB (640 words) - 11:58, 20 February 2013
  • ;1. Built example Table 1: Temperature ranges of the process medium and other parameters in the Mandr
    3 KB (408 words) - 11:59, 20 February 2013
  • ;1. Built example Table 1: Temperature ranges of the process medium and other parameters in the Tyras
    3 KB (418 words) - 11:59, 20 February 2013
  • ;1. Built example Table 1: Temperature ranges of the process medium and other parameters in the Stasi
    3 KB (430 words) - 12:00, 20 February 2013
  • ;1. Built example Table 1: Temperature ranges of the process medium and other parameters in the Manda
    3 KB (378 words) - 12:00, 20 February 2013
  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
    2 KB (337 words) - 12:25, 26 February 2013
  • 1. Systematics of SystemConcepts ::1. Generic system –SPO X – Water:
    809 B (114 words) - 12:35, 21 February 2013
  • {| border="1"
    1 KB (165 words) - 11:04, 30 December 2014
  • 1.) Systematics of SystemConcepts ::1. Generic system –SPO X – Water:
    544 B (73 words) - 10:51, 27 February 2013
  • ;1. Systematics of SystemConcepts ::1. Generic system –SPO X – Water:
    883 B (122 words) - 13:00, 26 February 2013
  • ::1. Generic system –SPO X – Water:
    618 B (78 words) - 11:10, 27 February 2013
  • ::1. Generic system –SPO X – Water:
    475 B (60 words) - 11:23, 27 February 2013
  • ::1. Generic system –SPO X – Water:
    446 B (56 words) - 11:27, 27 February 2013
  • 1.) Systematics of SystemConcepts ::1. Generic system –SPO X – Water:
    533 B (73 words) - 14:08, 26 February 2013
  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
    4 KB (571 words) - 12:31, 21 February 2013
  • 1.) Systematics of SystemConcepts ::1. Generic system –SPO X – Water:
    531 B (73 words) - 14:10, 26 February 2013
  • {| border="1"
    988 B (116 words) - 18:28, 14 January 2015
  • {| border="1" {| border="1"
    3 KB (341 words) - 12:47, 21 February 2013
  • 1.) Systematics of SystemConcepts ::1. Generic system –SPO X – Water:
    549 B (75 words) - 11:14, 27 February 2013
  • ;1. Systematics of SystemConcepts ::1. Generic system – NSO - Air :
    587 B (82 words) - 11:16, 27 February 2013
  • ::1) [[Powdered milk production]]
    644 B (72 words) - 12:29, 21 November 2012
  • {| border="1"
    988 B (114 words) - 12:34, 26 February 2013
  • {| border="1"
    1 KB (132 words) - 10:56, 27 February 2013
  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
    1 KB (189 words) - 12:02, 20 February 2013
  • '''1. Systematics of SystemConcepts''' ::1. Generic system – NPC :
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  • ...purified juice is a sugar solution containing approximately 14% sugar and 1% non-sugars. It is now necessary that this solution is thickened up into a Figure 1: Sugar evaporation general flowsheet. LITERATURE: http://www.monitorsugar.c
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  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of instant coffee production:
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  • {| border="1" ...offee||align="center"| 100 - 110||||align="center"| steam||align="center"| 1-4h||||
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  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of decaffeinated coffee production:
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  • ...l chambers. The residence time in the blancher can vary from approximately 1 to 5 minutes depending on the fruit or vegetable being blanched. For some p ...t, or the drum blancher with counter current water cooling, which produces 1 to 2.6 kWhe/t of frozen product (European Commission, 2006)
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  • '''1. Systematics of SystemConcepts''' ::1. Generic system – NPC :
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  • ...t 60°C (140°F) for 1 minute. It was defined in 1951 by Del Vecchio et al,1 and is employed in rating the effectiveness of pasteurization processes for <blockquote>'''PU = t × 1.393 (T − 60)'''</blockquote>
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  • ;1. (a) General Flowsheet of short time pasteurized milk: Figure 1: Short time pasteurized milk process LITERATURE: BAT for Food, Drink and Mi
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' Figure 1: Direct vs indirect continuous sterilization LITERATURE: http://www.foodsci
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  • <br/>'''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ...ems were estimated to be $0.25/barrel ($0.2/hl), compared to $1.7/barrel ($1.4/hl) for tunnel pasteurizers (Dymond, 1997). Since flash pasteurization is
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  • ...reak down protein during this stage). Ramp up to 65°C and hold for approx 1 hour (starch gelatinises and breaks down in sugars). Finally ramp up temp t Figure 1. Typical triple decoction mashing process (Hind, 1950) : solid line = tempe
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' Figure 1: Malt pre-heating in a kiln
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  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
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  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
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  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
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  • {| border="1" ...h'''||||||||||||containing: NaOH: 3%, surfactant: 0.2-0.4%, sequestrant: 0.1-0.2%||Chemistry and Technology of Fabric preparation and finishing
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' 1. Run fabric in a bath containing :
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ...it is gravity-settled and the settled liquor partly recycled to scour bowl 1 and partly discharged. Flocculant may be added to the heavy solids settling
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ...ubstances from previous operations, with a minimal elimination of sericin (1 – 2 %), so that the fabric keeps the characteristic stiff-handle. The ope
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  • {| border="1" ...solution containing 6 – 8- % of mineral acid (generally sulphuric acid), 1-2 g/l detergent|| align="center"| wool carbonising
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ...Rinsing. c. Immersion in a long bowl containing 5-7% (w/v) sulphuric acid, 1-2 g/L detergent at 20-30oC. d. Double squeezing and/or continuous centrifug
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ''1) Development and Application of a practice for high-speed Mercerisation of
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ;1. Polyester/Cotton
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ''1.) Plasma treatment''
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  • {| border="1" ...le="background:#AACCEE;"| Steaming|| align="center"| 120|| align="center"| 1|| |||||| align="center"| temperatures vary with quality|| align="center"| 2
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ...ounts of processing oil. Inadequate removal (Woolmark recommends less than 1.5% by weight Total Fatty Matter remaining), can lead to increased soiling,
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ''1.) Enzyme catalysed finishing treatment:''
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  • {| border="1" ...g mill|| align="center"| 70-120|| align="center"| 11-18|| align="center"| 1-2|| align="center"| BAT in textile industry 2003
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  • {| border="1" ...g mill|| align="center"| 70-120|| align="center"| 11-18|| align="center"| 1-2|| align="center"| BAT in textile industry 2003
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  • {| border="1" ...le="background:#AACCEE;"| shorttimebleaching|||||| align="center"|steam|| 1-3min|||| align="center"| with H2O2 in open steamers with overheated steam||
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ...is unstable as a gas and can only be stored as a solution of approximately 1% in water, it must be generated on-site as an aqueous solution. There are t
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ::1.) pre-bleaching at pH 11.5 in bath
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' :1. removing the unfixed dye by washing with complexing agents or surfactants
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' :1. removing the unfixed dye by washing with complexing agents or surfactants
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  • {| border="1" ...||| align="center"| 1,8-2,5|||| align="center"| 90 min|| align="center"| 1:1 metalcomplex dyes
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ::* 1:1 and 1:2 metal complex
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  • {| border="1" ...||| align="center"| 1,8-2,5|||| align="center"| 90 min|| align="center"| 1:1 metalcomplex dyes
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' Silk is dyed with the same dyes as wool, excluding 1:1 metal complex dyes. In addition, direct dyes can be used. The dyeing pH is
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ::* acid or 1:2 metal-complex dyes (pH 5-8)
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT'''
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ...e groups NH-CO and NH2 – in the polymer chain, acid, basic, reactive and 1:2 metal-complex dyes (ionic) can also be used. However, in practice acid le
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ;1.) Cleaning of the fibre-material
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ;1.) direct printing
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  • 1) Riedel Oberflächentechnik Bielefeld GmbH, Bielefeld
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  • {| border="1" ...HR Steel|| align="center"| 70|||| align="center"| Mix of 10-18% nitric and 1-5% hydrofluoric acids
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  • {| border="1" ...HR Steel|| align="center"| 70|||| align="center"| Mix of 10-18% nitric and 1-5% hydrofluoric acids
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  • {| border="1" | style="background:#AACCEE;"| Tin stripping of PCB: Stage 1|| align="center"| 25-35|||| align="center"| 20-60 sec|| align="center"| hyd
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  • {| border="1" ...er"| air || align="center"| continious || align=”center”| || rowspan="1" align="center"| Risse, A. (2012). Leiterplattentechnologie. In Fertigungsv
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  • {| border="1" ...Accelerator, '''5.''' Stabilizer, '''6.''' Surfacant|| align="center"| '''1.''' 19-26 g/l, '''2.''' 23-30 g/l, '''3.''' 30-50 g/l. '''4.''' 2-4 g/l, ''
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  • {| border="1" ...acid, '''4.''' Distilled Water|| align="center"| '''1.''' 5-5,8, '''2.''' 1, '''3.''' 8|| align="center"| 15-20 min|| align="center"| pH:5-6(optimum)||
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  • {| border="1" | align="center"| 1-3 min|| align="center"| spaying or dipping of individual parts
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  • ...oilers sharing an exhaust gas recuperator. Here the smaller boiler (boiler 1 which produces 80 tonnes steam/hour) is mainly used in summer and the large ''1. Green chemistry:''
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  • ''' 1. Use of power and steam from cogeneration plants''' ...y applicable for consumers of a vast amount of energy as the data in Table 1 show.
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  • '''1. OBJECTIVE''' 1. The '''first method''' is based on the production of a vapour by boiling t
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  • '''1. OBJECTIVE''' The specific heat of PER (the solvent most commonly used) is about 1/5 of that of water and the latent heat of evaporation is over 10 times lowe
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  • '''1. OBJECTIVE''' ...operations will be 2.4 g/l. Conversely, if the liquor ratio is reduced to 1:7, Cf becomes 26 g/l and 11 g/l, respectively, for one and two subsequent r
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  • '''1. OBJECTIVE''' ''1. Techniques for the removal of starch-based sizes''
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  • '''1. OBJECTIVE''' ...a long time; other enzymes are still the object of investigation. Table 6.1 lists the main enzymatic processes already in use or currently emerging in
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  • '''1. OBJECTIVE''' 1) hydrogen peroxide (H2O2)
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  • '''1. OBJECTIVE''' ...iquor. So, for example, a liquor ratio of 1:10 means 10 litres of water on 1 kg textile material. This parameter influences the amount of water and ener
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  • '''1. OBJECTIVE'''
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  • {| border="1" | style="background:#AACCEE;"| Tin stripping of PCB: Stage 1|| align="center"|25-35|| align="center"| || align=”center”|20-60 sec||
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  • {| border="1" ...al colouring|| align="center"| 25|| align="center"| || align=”center”| 1/2-5 min|| align=”center”| Acid solutions containing metal salt (usally
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  • ...t (AC) is applied. This deposits oxide of the other metal which penetrates 1 – 5 μm deep into the pore of the alumina, with the residual oxide layer
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  • ...yanide-based electrolyte is 4 – 10 g/l of stannate, 4-20 g/l copper, and 1 – 4 g/l zinc, with 6 – 10 g/l potassium cyanide. It is used in two diff
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  • {| border="1" ...-600 g/l of the tetrahydrate salt; boric acid: 35-45 g/l; nickel chloride: 1-15 g/l||
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  • ...called “chrome plating”. They consist of a very thin chromium topcoat (1%) over an undercoat of nickel (99%). Nickel provides a very smooth, brillia
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  • {| border="1" ...luoride- free|| align="center"| Chromic acid: 180-350 g/l; sulpahte ions: 1,8-6 g/l; mixed sulphate and fluoride ions: <2% of the content of the chromi
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  • ...by bright nickel undercoats. Deposit thickness is generally in the range 0.1 – 0.4 μm, with a treatment time from 2 to 13 minutes. The finish has a t ...520 g/l) and catalysts (nitrates, fluorides). The layers are porous and <1 μm.
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  • {| border="1" ..."center"| || align=”center”| || align=”center”| Alloys: zinc/iron(<1%) from alkaline cyanide-free electrolytes; zinc-cobalt(<3% Co) from acid or
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  • ::* zinc/iron (<1% Fe), from alkaline cyanide-free electrolytes
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  • ...ruthenium and platinum) have also been developed. Thin layers of less than 1 μm are used to make a wide range of items appear valuable without commensu ...g/l but may use gold (III) potassium cyanide (KAu(CN)4) at a pH of around 1. These are often used on difficult to plate base materials such as stainles
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  • ...um carbonate. Cadmium may be present in some formulations as a brightener, 1-5 mg/l giving approximately 0.03% in the deposit. Lead may be used in some
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  • ...res of electric motors, generators or transformers. A phosphate coating of 1 – 6 μm thickness is sufficient insulation to prevent eddy currents. ...es both thin-coating (0.2 – 0.4 g/m2) and thick-coating methods (0.6 – 1.0 g/m2). The colour of the layers is blue-green, but may be reddish iridesc
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  • '''1. GENERAL INFORMATION''' ''Figure 1: Input vs Output''
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  • '''1. Introduction''' ''Figure 1: General flow diagram for fish processing''
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  • '''1. Case study or built example''' Figure 1: Process flow chart of the operation
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  • '''1. Introduction''' Figure 1: Flow diagram of slaughtering pigs
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  • '''1. Case study or built example''' Cleaner production assessment was carried out in a Danish abattoir. 1.1 million pigs are processed every year. They are delivered in trucks, each c
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  • '''1. Case study or built example''' ;''1. Better emptying of production tanks''
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  • Table 1: Specific energy required (MJ/t) to chill, freeze and process (cutting and Figure 1: Flow chart Inputs and Outputs for cooling systems
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  • '''1. Description of techniques, methods and equipment'''
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  • '''1. Description of techniques, methods and equipment''' Figure 1: Inputs and Outputs for dehairing of pigs
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  • '''1. GENERAL INFORMATION''' ;1. Reduction of the resource consumption
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  • '''1. Cleaner Production opportunities''' ''Table 1: Barriers to the implementation and diffusion of CP''
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  • '''1. Type''' ''Figure 1: Processes and sources of waste in the company''
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  • '''1. Sources of pollution''' ::1. Quality Control for Raw Materials
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  • '''1. Type''' :1. in water savings and
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  • '''1. DEFINITION & OBJECTIVE''' ''Figure 1: PI technologies''
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  • '''1. DEFINITION & OBJECTIVE'''
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  • <br/>'''1. General information'''
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  • '''1. General description of the company'''
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  • '''1. General description of the company''' ...Portugal could reduce the quantity of raw material lost from 2 percent to 1 percent. It has also cut the amount of water used by 4 cubic meters per cub
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  • '''1. GENERAL DESCRIPTION'''
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  • *Processing time is usually much less than 1 day for hot smoking and drying ...verall heat transfer coefficient of the smoker/drier should be ~3 W m-2 K-1
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  • '''1. GENERAL DESCRIPTION''' ;1. General Flowsheet of soft drink production
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  • == 1. GENERAL DESCRIPTION: == ;1.1 General Flowsheet of bread production:
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  • == 1. GENERAL DESCRIPTION: == ;1.1 General Flowsheet of cake production:
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  • == 1. GENERAL DESCRIPTION: == ;1.1 General Flowsheet of cereal production:
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  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet for pig slaughtering:
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  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet for cattle slaughtering:
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  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of chocolate production:
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  • '''1. GENERAL DESCRIPTION:''' ;1. General Flowsheet of coffee production:
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  • == 1. GENERAL DESCRIPTION: == ;1.1 General Flowsheet of biscuits, cookies and crackers production:
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  • '''1. DEFINITION & OBJECTIVE''' Figure 1: Connection between CP and EE, Literature: van Berkel, R.
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  • '''1. GENERAL INFORMATION'''
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  • ;1. Solar Heat and Solar Thermal Technologies
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  • ...age might end up being able in order to save a person cash. </P><P>Another 1 of the particular numerous factors why you ought to request a minumum of on
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  • '''1. OBJECTIVE'''
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  • '''1. OBJECTIVE'''
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  • '''1. OBJECTIVE'''
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  • {| style="text-align:center" border="1"
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  • '''1. Type''' ...://en.wikipedia.org/wiki/Chemical_oxygen_demand COD] during production are 1.15 million tons respectively 2.2 million tons which represents 18% and 12.5
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  • '''1. Introduction''' :1. Primary production of milk on farms: These mainly apply keeping of animal
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  • ;1. Definition: (BAT for Food, Drink and Milk Industries, June 2005) Figure 1: Process flow diagram for ice cream manufacture
    9 KB (1,475 words) - 09:33, 6 August 2013
  • ;1. General Flowsheet of soup pasteurization: Figure 1: Soup pasteurization.
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  • ;1. General Flowsheet of ready meals production:
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  • ;1. Built example Figure 1: Flowsheet of built solar system in Gangl industry LITERATURE: AEE INTEC
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' Figure 1: Sugar drying process LITERATURE: [http://www.monitorsugar.com/htmtext/btin
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' ::Figure 1: Spray-drying tower.
    4 KB (668 words) - 13:15, 30 August 2013
  • '''1. OBJECTIVE''' :*High heat short time pasteurisation (HHST): 85 – 90oC, 1 - 25sec
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  • '''1. DESCRIPTION OF TECHNIQUES, METHODS AND EQUIPMENT''' Figure 1: Time/temperature curve for the inactivation of Mycobacterium tuberculosis
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  • '''1. OBJECTIVE''' ...f the tubes is of the order of 15:1. The basket evaporator shown in Figure 1(a) is a variant of the calandria evaporator in which the steam chest is con
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  • <br/>'''1. OBJECTIVE''' ...p://www3.interscience.wiley.com/cgi-bin/abstract/109062827/ABSTRACT?CRETRY=1&amp;SRETRY=0])
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  • '''1. OBJECTIVE'''
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  • 1. OBJECTIVE 1. Concentration
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  • '''1. OBJECTIVE'''
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  • <br/>'''1. OBJECTIVE'''
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  • '''1. OBJECTIVE'''
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  • '''1. OBJECTIVE''' ...l chambers. The residence time in the blancher can vary from approximately 1 minute to minutes depending on the vegetable or fruit being blanched.
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  • '''1. OBJECTIVE''' ...on cycle of 3-5 minutes reduces residual moisture content to approximately 1,0 l/kg dry fibre (in the case of wool).
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  • {| style="text-align:center" border="1" cellpadding="2"
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  • {| border="1" style="text-align:center" cellpadding=2
    3 KB (277 words) - 14:51, 17 December 2013
  • | 1 page summary
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  • <br/>'''1. Description of techniques, methods and equipment'''
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  • Figure 1: Inputs and Outputs for cleaning
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  • '''Address:''' Zaunergasse 1-3 – 1030 Wien – Austria '''Phone: '''+43 1 712 21 21 23
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  • == VECC France (1) ==
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  • 1.'''Spray drying''':
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  • 1.'''Microwave pasteurization''':
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  • 1.'''Radiation'''
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  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    6 KB (997 words) - 14:00, 15 March 2015
  • ...ge. There are four primary components to the typical refrigeration system: 1. the compressor , 2.The condensor, 3. The expansion valve, and 4. The evapo
    2 KB (339 words) - 14:09, 6 December 2014
  • ;Figure 1 Process Intensification- An overview ;1. "Maximize the effectiveness of intra-and intermolecular events
    4 KB (555 words) - 10:15, 1 September 2014
  • ;Figure 1 Overview of Emerging Technologies
    3 KB (425 words) - 10:24, 1 September 2014
  • ;'''1. Concentration of product''' ...round of the five-stage BVs a solids concentration of 35% and goes out of 1,800 kg / h from the evaporator. This concentrate is stored in a concentrate
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  • ;1. Concentration of product '''1.1Thermal concentration'''
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  • ;Figure 1 D value of certain microorganisms in the pasteurization or sterilization of
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  • ;1.Thermal pasteurization ;Figure 1 D value of certain microorganisms in the pasteurization or sterilization of
    8 KB (1,256 words) - 18:47, 14 January 2015
  • '''1.Flate plate Collectors:''' '''Figure 1: Specific cost analysis of flat plate collectors'''
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  • '''1.Specific Cost Analysis of Water- Water Heat Exchangers''' '''Figure 1: Specific cost anlaysis of Water- Water Heat Exchangers'''
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  • ...have to be made. The status check is subsidised with 75% of the costs, but 1,000 Euro maximum. For the other measures the funding is between 15% and 35% ...trical power output of roughly 1 kW) for private customers with a grant of 1,000 Euro.
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  • ...(H2O-LiBr) for water cooling; re-cooled with water (example temperatures) [1] Table 1: Characteristics data of absorption chillers for the production of chilled
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  • ...ort application must be modulated to prevent over heating the make up air [1]. ...bustion process. For every 22ºC reduction in the gas temperature there is 1% saving fuel in the boiler [3].
    22 KB (3,422 words) - 11:48, 30 December 2014
  • ...hasis on the Efficient Use of Energy and reducing Environmental Effects”[1]. It joins basically all the technologies that can help minimize energy con Figure 1: Example of pinch integration [1]
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  • Source: adapted from VDI 2592 Port 1, Emission control, Plants for extracting vegetable oils and fats
    2 KB (298 words) - 11:41, 21 November 2014
  • ...iz et al. 2011 showed a maximum orange peels specific biogas production of 1,100 L/KgTS. The complete orange degradation is achieved after 11 days. The
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  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    3 KB (470 words) - 14:21, 19 February 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,797 words) - 13:03, 23 January 2015
  • Illustration 1: Shell and tubes heat exchanger [1] Illustration 1: Plate and Plate-Fin heat exchangers [5]
    3 KB (475 words) - 14:28, 17 March 2015
  • Illustration 1: Shell and tubes heat exchanger [1] Illustration 1: Plate and Plate-Fin heat exchangers [5]
    3 KB (445 words) - 14:25, 17 March 2015
  • Illustration 1: Shell and tubes heat exchanger [1] Illustration 1: Plate and Plate-Fin heat exchangers [5]
    3 KB (449 words) - 13:09, 17 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    14 KB (1,823 words) - 13:30, 23 January 2015
  • <br/>'''1. GENERELL INFORMATION''' ...ividual zones of the multistage bottle cleaning process are the following: 1)soak, 2)caustic bath, 3)1st zone of hot water tank, 4)2nd zone of hot water
    7 KB (1,011 words) - 17:58, 25 February 2015
  • ...r countercurrent flows. The plate heat exchanger efficiency is around 75% [1]. Illustration 1: Plate and Plate-Fin heat exchangers [2]
    2 KB (369 words) - 13:12, 19 February 2015
  • Illustration 1: Tubular heat exchanger [1] [1] Fundamentals of Heating Systems. ASHRAE
    3 KB (508 words) - 13:28, 19 February 2015
  • ...unable to grow, multiply or function in the absence of sufficient water. [1] Illustration 1: Rotatory Wheel heat exchanger [4]
    3 KB (502 words) - 13:50, 19 February 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    10 KB (1,538 words) - 20:10, 4 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,787 words) - 13:29, 23 January 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    8 KB (1,261 words) - 20:11, 4 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,774 words) - 13:32, 23 January 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    5 KB (705 words) - 14:01, 15 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,762 words) - 13:26, 23 January 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
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  • ...all along the line, breweries have usually industrial-sized energy needs [1]. Energy is needed for the production of beer, but also clean resources li '' Figure 1: Environmentally-friendly beer production in Murau [3][7]''
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  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    5 KB (702 words) - 13:58, 15 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,769 words) - 13:29, 23 January 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    12 KB (1,849 words) - 20:01, 4 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,777 words) - 13:25, 23 January 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    32 KB (4,740 words) - 10:42, 30 March 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    14 KB (2,146 words) - 19:49, 4 March 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    12 KB (1,767 words) - 19:41, 4 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    32 KB (4,761 words) - 10:45, 30 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    32 KB (4,739 words) - 10:43, 30 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    32 KB (4,741 words) - 10:44, 30 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,764 words) - 13:27, 23 January 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    32 KB (4,726 words) - 10:43, 30 March 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,763 words) - 13:27, 23 January 2015
  • ...the distribution of the energy consumption for a typical baking facility [1][2][3]. '' Figure 1: Energy consumption distribution of bakeries [4] ''
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  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,754 words) - 13:31, 23 January 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
    13 KB (1,754 words) - 13:28, 23 January 2015
  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
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  • |1. Reduce excess combustion air to minimum |1. CO2/O2 measurement
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  • Figure 1: Conventional Drying of whey
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  • ...ng and evaporation of the wort (about a 4-8% evaporation rate) over a 1 to 1.5 hour period. Wort boiling has a number of aims: to sterilize and stabili ...n vessel, the wort is kept at 100°C with almost no evaporation (less than 1%). In this step all processes that involve heat treatment are performed (fo
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  • Annual data for EU maltsters (2006)1:
    4 KB (658 words) - 13:50, 17 February 2015
  • Illustration 1: Shell and tubes heat exchanger [1] [1] Fundamentals of heat and mass transfer. Incropera, DeWitt, Bergman, Lavine
    2 KB (262 words) - 17:58, 12 May 2015
  • <br/>'''1. GENERELL INFORMATION''' ...ividual zones of the multistage bottle cleaning process are the following: 1)soak, 2)caustic bath, 3)1st zone of hot water tank, 4)2nd zone of hot water
    7 KB (1,011 words) - 09:30, 28 February 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    8 KB (1,102 words) - 20:02, 4 March 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    11 KB (1,610 words) - 20:08, 4 March 2015
  • ...umped to the section where bottles enter the main caustic bath (scheme No. 1). At this point of the bottle washing machine, the highest temperature is r
    6 KB (877 words) - 20:13, 4 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    32 KB (4,770 words) - 10:41, 30 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    31 KB (4,717 words) - 10:42, 30 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    31 KB (4,717 words) - 10:44, 30 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    31 KB (4,717 words) - 10:45, 30 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    31 KB (4,717 words) - 10:45, 30 March 2015
  • ...n routes of biomass are used to convert biomass into biogas or bioethanol [1]. Figure 1: Wood pellet combustion system [6]
    31 KB (4,717 words) - 10:46, 30 March 2015
  • Illustration 1: Shell and tubes heat exchanger [1] Illustration 1: Plate and Plate-Fin heat exchangers [5]
    3 KB (407 words) - 13:11, 17 March 2015
  • This handbook is designed for the '''Energy Audit Support Tool 1.0'''. Here you can find the Download Link: [https://www.energymanager.eu/en :*<u>Version 1</u>: The original version. It is now closed. No branch is selected. It can
    64 KB (9,851 words) - 12:31, 26 April 2019
  • Illustration 1: Shell and tubes heat exchanger [1] Illustration 1: Plate and Plate-Fin heat exchangers [5]
    3 KB (407 words) - 13:10, 17 March 2015
  • Illustration 1: Shell and tubes heat exchanger [1] Illustration 1: Plate and Plate-Fin heat exchangers [5]
    3 KB (407 words) - 12:39, 17 March 2015
  • Figure 1: Information content of technology description
    8 KB (1,219 words) - 09:50, 20 July 2016
  • ...gas and consists of hydrogen, carbon monoxide, carbon dioxide and methane [1]. Producer gas is in most cases currently used as a fuel for heat and power [1] Balat, M., Balat, M., Kirtay, E., & Balat, H. (2009). Main routes for the
    2 KB (309 words) - 10:16, 19 March 2015
  • ;Figure 1 Process Intensification- An overview ;1. "Maximize the effectiveness of intra-and intermolecular events
    4 KB (555 words) - 11:59, 13 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    5 KB (702 words) - 14:10, 15 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    4 KB (689 words) - 14:11, 15 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    4 KB (689 words) - 14:11, 15 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    4 KB (689 words) - 14:12, 15 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    4 KB (689 words) - 14:12, 15 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    4 KB (689 words) - 14:12, 15 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
    4 KB (689 words) - 14:13, 15 March 2015
  • ...r to close to the acid dew point before it enters the economiser.Typically 1% of fuel use is saved for every 25 degrees celsius reduction in exhaust gas
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  • ...tion process and the formation of glycerin as by-product in biorefineries [1][2][3]. Table 1: Technical specifications of biodiesel production
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