TOMSA DESTIL ® is a Spanish company specialized in the engineering and manufacturing of alcohol distillation plants and related products in the international market. Equipped with highly experienced personnel, TOMSA is reputed for having substantially improved the processes for producing alcohol, with a view to obtaining the best possible product at the lowest operating cost. TOMSA´s engineering capabilities are coupled with its ability to design and build equipment for each and every specific production area of the distillation process. TOMSA DESTIL ® is a "Turn-key" engineering and manufacturing company for every single aspect of the alcohol distillation process. In the early 1970´s, TOMSA DESTIL ® was one of the pioneers in the development and commissioning of the vacuum distillation system (Multipressure system.) As a result of this, TOMSA rapidly expanded in the international market, building distilleries in all five continents of the world, gaining experience with all types of raw materials. In the production of all the different types of alcohols (fuel alcohol, industrial alcohol and potable alcohol), TOMSA DESTIL ® offers its know-how, to producers of each and every aspect of the alcohol manufacturing process and associated services and utilities. TOMSA´s equipment and process designs uses the latest "state of the art" methods adapted to suite each customers particular requirements in such a way that enables TOMSA to be a flexible supplier to all of its individual customers.

ACTIVITIES

Storage and Handling of Raw Feeds

Mash Preparation for:

Molasses

Starch Products (maize, potatoes, agave, etc.)

Fruits (grapes, cherries, apples, etc.)

Continuous or Incremental Fermentation

Atmospheric or vacuum distillation to obtain:

Super fine alcohol

Spirits

Dehydrated Alcohol

Acetic Acid, biochemical or catalic

Treatment of Wastewaters and By-products

Evaporators, Driers, Decanters and Reactors

Molecular sieves for the dehydration of alcohol

Extractive distillation, distillation of essential oils

Distributed Digital Control; Adaptive- Predictive Control

WHAT CAN WE OFFER?

The latest technology in Fermentation and

Distillation

In house Engineering and construction

Operating Know-how of distilleries

Free technical assistance for 5 years (*)

From consultant service to…

Iso-9001 Quality controls

ALSO Market Studies

Training and Teaching

R+D service for customers

Private laboratories for investigation

Periodical technical reports

(*) Engineers and technicians fees

THE ALCOHOL DISTILLERY

The production of alcohol using the different types of raw feeds generally

includes five stages, each one is composed of a group of equipments or

units which are named "Section".

S-200.- Discharge and Storage of the raw feed.

S-300.- Mash preparation

S-400.- Fermentation

S-500.- Distillation

S-600.- Storage of Finished Products

In addition, the Distillery requires a minimum of General Services which

provide the utilities needed:

Civil works and buildings, steam generation, fuel storage, acquisition

and treatment of water, production of compressed air, waste water

treatment, electrical installation and lighting, quality control

laboratories, maintenance workshop and fire protection installation.

TOMSA DESTIL can provide the preliminary study, the engineering

project, the construction or supply completely these Sections and

General Services required by a Distillery.

TYPICAL DISTILLATION COLUMN

A typical distillation column must be equipped with the necessary auxiliary equipment andinstrumentation for its correct operation and control:

1.-Adequate design of the internal components with special dedication to the hydraulic design ofplates and their mass transfer efficiencies. 2.-Correct selection and design of the heating system for the column (reboiler, direct steam, etc.)and the condensation section for the head vapours. 3.-Automatic control and regulation system, with the optimum selection of the instrumentation type required, location of the most sensitive zones to minimize perturbations of the system and the most adequate control logic for the process.

MOLASSES MASH PREPARATION

PROCESS "HYMOL"

Every fermentation process requires previously a preparation of the substrate to be fermented aswell as adjustments to the state of the raw material to adapt to the requirements of the cellularmetabolism of the yeast. The "HYMOL" process designed by TOMSA for the case of molasses, starts with a precise controlof the feed rate of the incoming molasses and its pre-dilution with water (flows 1 and 10) in continuous static mixer "MX 313". It is preheated in a counter current flow heat exchanger "E-350" using the pasteurized mash. Afterwards this mash is pasteurized to 95ºC using direct steaminjection in "E-310". After filtration, addition of nutrients and correction of pH, it is cooled off anddiluted to the required concentrations for the aerobic fermentation, (flow 9) and anaerobic, (flow 7). The process is continuous and is completely automated.

STARCH MASH PREPARATION

"HYMIDO" PROCESS

An extensive variety of amylaceous cultures as raw material for the alcohol production can be used (maize,potato, tapioca, etc.) The local climatology, the quality of the soil, the crop resistance and the ease in handling are, in addition to the starch content, the important criteria when selecting the raw feed to be used. TOMSA DESTIL offers a continuous hydrolysis and saccarification process using a Jet-cooker based on consuming the minimum amount steam due to the use of high substrate concentrations and optimizing theusage and transfer of heat at the different stages of heating and cooling the mash. At the same time, theproductivity of the fermentation is improved substantially as a result of maximising the pre-saccarification of the starch before going into the fermentation vats. First, the raw material has to be suitably cleaned. All foreign and non desirable objects which could seriouslydamage the equipment must be removed, such as sand, metal objects, etc... Afterwards, the starch is mixed with hot water and undergoes a partial hydration. This "gelatinisation" produces a viscous mash which must betreated with thermally stable alpha-amylase enzymes to transform the starch into dextrins. This process, called "liquefaction" reduces the viscosity of mash and avoids the precipitation of the starch or formation of gels in thesubsequent stages of the process when the temperatures are reduced. Actually the gelatinisation and the liquefaction occur practically at the same time, and are collectively called "cooking" Finally, before fermenting the sacharification of the dextrins with glucose-amylase enzymes is performed at an average temperature of 60º before finally cooling the mash down in order to go on to the fermentation. TOMSA DESTIL performs in its laboratories, a case by case study into the specific requirements of eachdistillery, determining the expected yields for each type of raw material the client may use.

10

FERMENTATION

The processes of alcoholic fermentation can be classified into two groups: continuous or discontinuous,and within each group there are two different types of processes depending on whether the process ofyeast production is with a "mother vat" or with "yeast recycling" (the Melle Boinot process and others).TOMSA DESTIL has developed the technology for all these processes obtaining the highesttransformation yields of alcohol from sugar. This is in a large part due to the techniques of the TOMSA microbiological laboratories in selecting and improving the “saccaromice cerevisae” yeast strain.

PROCESS USING A MOTHER VAT: "PRO-YEAST"

This consists of continuously generating yeast, from a low concentration mash. The yeast which will beused later for the alcoholic fermentation is not recovered or recycled. Mother vats are continuously fed with air (aerobic fermentation). The fermented solution produced will becomposed of a biomass rich in yeast which will be sent to the fermentation vats under the name of "yeast foot". The fermentation vats of volumes, greater than the mother vats, are exempt of air (anaerobic fermentation)and they are fed with a high concentration mash after the yeast foot has been added. If the chosenprocess is discontinuous, there will be several fermentation vats, operating intermittently in accordance tothe classic sequence: addition of yeast foot, filling, termination, followed by distillation. On the contrary, if the process selected is continuous, there will be one or more vats in series in a cascade fashion, such that the first one continuously receives a flow of yeast foot and mash and the last vat willhave completely fermented mash continuously leaving for the distillery. In all the cases the fermentation process produces heat (exothermic reaction) and for this reason theremust always be a cooling system for the vats.

PROCESS WITH YEAST RECYCLING: "HY-YEAST"

In this case the yeast foot is substituted by the yeast cream obtained from passing the fermented mashthrough a centrifuge separator before distilling it. Depending on each specific case, this yeast cream couldundergo a revitalisation treatment before returning to the fermentation vats. In this case the yeast foot produced, usually has a smaller volume than that when using the mother vatprocess. However it is far richer in yeast biomass. In all the cases the fermentation produces a substantial volume of CO2, of a food grade quality that can be recovered for liquefaction and sale.

PROCESS WITH STILLAGE RECYCLING: "STILL-YEAST"

This process allows fermenting sweetened mash reusing part of the stillage from the distillation sectionincluding all its solid content. This is to replace part of the dilution water and has three fundamental aims: a) To substantially reduce the volume of spent waste which the distillery has to treat (a smaller net volume ofstillage); b) to reduce the bacterial infections due to the bacteriostatic effect of the high solid concentrationon the fermenting mash; c) to reduce the consumption of nutrients and acid, required by the yeast forgrowth and pH balance. Achieved because of the unused salts and acidity contained within the stillage. It is obvious that this new process requires a yeast strain different from the standard Saccaromices Cerevisae which has to be able to reproduce themselves within a medium which has a high osmoticpressure exerted on the cellular membranes. TOMSA DESTIL has located several wild yeasts able to resist these adverse conditions having modified and selected this specie for its perfect adaptation to different culture mediums.

" PROVAC PROCESS " (one or two columns)

Based on many years of experience and many distilleries in operation, TOMSA can provide the "PROVAC" process, as the most efficient method for producing crude alcohol with respect to low energy consumptionand simplicity of operation. One of the greatest advantages of our vacuum distillation systems usingfermented mash, is the complete elimination of scaling and solids settling on the elements inside thedistillation columns. The combination of our valve design and the special system of downcomer tubes within the column interiorallows it to operate with liquids containing high quantities of suspended solids (grape lees, molasses,cereals, etc.) without suffering from choking columns, as well as withstanding mash with high scaling properties or with high concentrations of carbonates and sulphates.

"HYDROVAC" PROCESS (three columns)

When we want to obtain rectified superfine alcohol from raw or impure alcohols such as headsand tails of previous distillations, the process "HYDROVAC" offers several advantages. It requiresa minimum consumption of energy due to the use of a multi column system operating at differingpressures in order to obtain a cascade distillation. The system is able to produce alcohol of thehighest quality (organoleptic characteristics and purity) because of the advanced TOMSAtechnology in the process of elimination of impurities, heads and hybrid impurities using ahydroselection column and methanol separation in a demethylizer column. Obtaining in bothcases extractions with high impurity concentrations and so producing minimum volumes of technical alcohol extracted as by-product. .

"STILLVAC" SYSTEM (two columns)

With the STILLVAC system TOMSA provides the best technological solution for producing rectified alcohol ofhigh degree (upto 96.5 ºGL) from fermented mash within the typical quality parameters for the production ofbioethanol or beverage alcohols for maturing (rum, whiskey, brandy, tequila) The process makes use of all the advantages of "PROVAC" system in terms of vacuum distillation forfermented mash, since the mash column operates under a vacuum. In addition there is an extra energy saving that is achieved by having the rectifying column operate under pressure which enables the two columns to workas a dual effect using the vapours from the head of the rectifier (high temperature) to heat up the base of themash column (low temperature) without additional energy consumption required by this latter column. This heattransfer is achieved using a falling film reboiler. The whole process is commonly referred to the "multipressurecolumn system" The volatile impurities (heads) contained in fermented mash are eliminated from the zones at the head of eachof the column and the heavy impurities (tails) are eliminated both from the bottom of the mash column and from the central zone of the rectifying column. Depending on the type of raw feed used, the mash column reboiler will operate using stillage recirculation to produce the steam for the column or with spent lees (distilled water)obtained from the foot of the rectifying column, if there is a danger of scaling in the reboiler tubes.

.

SUPERFINE ALCOHOL FROM FERMENTED MASH

"FINEVAC" PROCESS

This is the combination of the PROVAC and the HYDROVAC processes properly readjusted to permit the production of mainly superfine alcohol from fermented mash using the minimum consumption of energy and the highest quality of rectified alcohol as required by the international liquor and cosmetics industries.

ANHYDROUS ALCOHOL (BIOETHANOL)

"DRYMOL" PROCESS

The most attractive and least expensive technique to dehydrate water-alcohol mixtures with concentrations in region from 93 to 96% vol. This method uses the adsorption of water in vapour phase by means of molecular sieves using a PSA (pressure-swing-adsorption) procedure. It is able to reach alcoholic concentrations of up to 99.9 % in volume. Like all the adsorption operations, the separation is due to the selectivity of the adsorbent solid (zeolites) to one of the components of the gas that crosses through it, in this case water, allowing the ethanol topass on and so dehydrating it. Industrial scale PSA systems are designed to continuously repeat the cycle of pressurization/adsorptionand depressurization/de-adsorption so that the process produces a continuous flow of dehydrated alcohol.This is possible by means of the using two or more zeolite reactors operating in an alternating fashion.

PROYECTO/PROJECT:

Planta de alcohol Superfino de Melazas (Llave en mano)Molasses Superfine Alcohol Plant (Turn-Key)

CAPACIDAD / CAPACITY:90.000 Lt /dia 90,000 Lt./day

CLIENTE / CUSTOMER :ALFICSA S.A.CienfuegosCUBA

AÑO FABRICACION / YEAR :2000

PROYECTO/PROJECT:

Planta de alcohol Superfino de Cereales

Molasses Superfine Alcohol Plant

CAPACIDAD / CAPACITY:15.000 Lt /dia 15,000 Lt./day

CLIENTE / CUSTOMER :GERMANY S.A.BucarestRUMANIA

AÑO FABRICACION / YEAR :1997

PROYECTO/PROJECT:

Planta de Fermentacion de Melazas, Caldera y T.Refrigeración

Molasses Alcohol Fermentation Plant, Boiler & Cooling Tower

CAPACIDAD / CAPACITY:30.000 Lt /dia 30,000 Lt./day

CLIENTE / CUSTOMER :SOTRAMEG S.A.KenitraMARRUECOS

AÑO FABRICACION / YEAR :1999

PROYECTO/PROJECT:

Planta de Hidrólisis y Sacarificacion de Agave (Tequila)

Hydrolisis & Saccharification Plant of Agave (Tequila)

CAPACIDAD / CAPACITY:400.000 Kg/dia400,000 Kg/day

CLIENTE / CUSTOMER :CASA CUERVO S.A.JaliscoMEXICO

AÑO FABRICACION / YEAR :2000

ADOLFO FDEZ. ALBARES SPAINÁGAVE DISTILLERIES SUDÁFRICAAGRALCO SPAINAGROCOMERCE BULGARIAAGROPAC MOROCCOAGRUP. ALC. BODEGAS COOP SPAINALCALIBER SPAINALCOHOLERA CHIBCHÓN SPAINALCOHOLERA DE ALMENDRALEJO SPAINALCOHOLERA DEL PUERTO SPAINALCOHOLERA PONCE OLMEDA SPAINALCOHOLERA SAN ISIDRO SPAINALCOHOL. VIN. DEL MEDITERRÁNEO SPAINALCOHOLERAS REUNIDAS SPAINALCOHOLES ANTICH S.A. SPAINALCOHOLES DE CANARIAS SPAINALCOHOLES DE HUELVA SPAINALCOHOLES DE TOMELLOSO SPAINALCOHOLES DE VALENCIA SPAINALCOHOLES DEL PORTILLO SPAINALCOHOLES PONS HERMANOS SPAINALCOHOLES VILLAFRANCA SPAINALCOHOLES Y DERIVADOS SPAINALCOHOLES Y DERIVADOS S.A. PANAMÁALCOHOLES Y DERIV. DEL VINO SPAINALCOHOLES Y GRASAS DE YECLA SPAINALCOHOLES Y VINOS SPAINALCOMASA SPAINALDEVISA SPAINALFICSA CUBAALGRY SPAINALITA LITUANIAALSAN SPAINALVIRESA SPAINANIS CASTELLANA SPAINANIS EL MONO SPAINANTICH S.A. SPAINANTONIO VALDERA SPAINAPV BAKER IBÉRICA SPAINASTUR PHARMA SPAINAZUCARERA DEL CARMEN SPAINAZUCARERA DEL GUADALFEO SPAINAZUCARERA EBRO AGRÍCOLA SPAINAZUCARERA MONTERO SPAINAZUCARERA ONÉSIMO REDONDO SPAINAZÚCARES Y ALCOHOLES PANAMÁBARCELÓ Y CÍA. CXA REP. DOM.BEECHAM SPAINBEPRONA SPAINBERE SPIRT RUMANÍABIOTECNOLOGÍAS APLICADAS SPAINBODEGAS IGLESIAS SPAINBODEGAS MONTBLANCHI, S.A. SPAINBODEGAS MONTERO SPAINBOD. ORTIZ Y FERNANDO DE TERRY SPAINBODGAS PABLO MARTÍNEZ S.A. SPAINBODEGAS Y DESTILERÍAS SPAINBRUGAL & CO. CXA REP. DOM.CAMPARI SPAINCARLE Y MONTANARI SPAIN

CASA CUERVO MÉXICOCASA MADERO MÉXICOCTRO. DE ALCOHOLES DEL PENEDÉS SPAINCERAS INDUSTRIALES SPAINCÉSAR PEREIRA PANAMÁCÍA. LICORERA DE NICARAGUA NICARAGUACISSA SPAINCIVINASA SPAINCLEMENTE CUESTA SPAINCLESA SPAINCOMPAÑÍA DE INDUSTRIAS AGRÍCOLAS SPAINCONSTAIN ECUADORCONSTRUCCIONES VENTO SPAINCOOP. DE BEZIERS FRANCECOOP. DE CIUDAD REAL SPAINCOOP. COMARCAL VALLE DE ALBAIDA SPAINCOOP. DEL CAMPO NUEVA ALCOHOL. SPAINCOOP. VINÍCOLA REQUENENSE SPAINCOVALSA SPAINCOVEN SPAINCOVIÑAS SPAINCRUZ CONDE SPAINCUBALCOHOL CUBACUBAS DE ROBLE ARGENTINADECOINSA SPAINDE SMET SPAINDELTOSA SPAINDESTILERÍA CHINCHÓN SPAINDESTILERÍA DE GUADALUPE SPAINDESTILERÍA DE MURCIA SPAINDESTILERÍA SERRALLES PUERTO RICODESTILERÍAS BENITO TORRES SPAINDESTILERÍAS DANUBIO SPAINDESTILERÍAS DE MURICA S.A. SPAINDESTILERÍAS DE OCCIDENTE SPAINDESTILERÍAS DE TOMELLOSO SPAINDESTILERÍAS DEL GUADALETE S.L. SPAINDESTILERÍAS LOS CAMICHINES MÉXICODESTILERÍAS M.G. SPAINDESTILERÍAS MAGISA SPAINDESTILERÍAS PERUANAS PERÚDESTILERÍAS SALAS Y SIRVENT SPAINDESTILERÍAS SYS SPAINDESTIL. Y CRIANZAS DEL WHISKY SPAINDIEGO LÓPEZ GARCÍA-GALLO SPAINDEULEP FRANCEDUPERIAL ARGENTINAEMPE S.A. SPAINEMPRESA DE LICORES DEL ESTADO ECUADORENGRACIO MOLLEJO MOLLEJO SPAINESCUELA T.S. INGENIEROS IND. SPAINETTEHADIED COMPANY IRÁNEUROCIENCIA SPAINFÁBRICA NACIONAL LICORES COSTA RICAFAQUIRESA SPAINFELIPE ESPINOSA S.A. SPAINFERNANDO CALAVID SPAINFERROVIAL SPAINFINOS DE ÁGAVE MÉXICOFLESUR SPAINFLORIDO HERMANOS SPAIN

FRADEALCO ARGENTINAFRANCISCO ARRANZ S.A. SPAINFRANCISCO CANTARERO SPAINFRANCISCO FERREIRA CALHAU PORTUGALGINÉS NAVAROO SPAINGLOBAL TRADE GMBH GERMANYGONZÁLEZ BYASS SPAINGRANDES BODEGAS SPAINHERCESA SPAINHERMANOS TORRES SPAINHIJOS DE FELIPE TORRES SPAINHIJOS DE J. ANTONIO PEINADO SPAINHIJOS DE V. CASAJUANA SPAINHIRAM WALKER EUROPA SPAINHUERTAS SPAININCAMASA SPAININD. DE LICORES DEL VALLE COLOMBIAINDUSTRIAL MAQUEDA S.A. SPAININD. RIBERA ANICOBA SPAININGENIO SAN NICOLÁS MEXICOINGENIO S. SEBASTIÁN MÉXICOINSTITUTO NAL. DE INVESTIG. SPAINISAÍAS FUENTES SPAINJAIME SOLER FIGUERAS SPAINJAIME VILA MONTANA SPAINJAVIER BALBUENA SPAINJESÚS RAMÍREZ SPAINJOAQUÍN CAMACHO Gª FILOSO SPAINJOAQUÍN P. BUSTILLO SPAINJONAS TORRES Y CÍA SPAINJUAN JOSÉ ORTIZ SPAINJULIÁN CHIVITE SPAINJULIÁN MAYORDOMO POZO SPAINJULIÁN PICAZO SPAINJUSTO MERINO SPAINLABORATORIOS LEO SPAINLABORATORIOS MADE SPAINLARIOS ECUADORLARIOS SPAINLENSA SPAINLIADE SPAINLICORES DEL NORTE SANTANDER COLOMBIALICORESA ECUADORLILLY SPAINLORENZO ALCÁNTARA SPAINMANUEL Gª DE LA CRUZ SPAINMANUEL V. LADRÓN DE GUEVARA SPAINMAQUIMPORT CUBAMAREX RUMANÍAMINAS DE ALMADÉN SPAINMINAZ CUBAMODERN CHEMICAL INDUSTRIES IRAKMOSTOS ESPAÑOLES S.A. SPAINNAVIDUL SPAINNUEVA ALC. DE UTIEL SPAINOLIVARERA EXTREMEÑA SPAINORENDAIN MEXICOOVIONES S.A. PORTUGALPEDRO DOMECQ SPAINPEDRO DOMECQ MÉXICOPEDRO DOMECQ COLOMBIA COLOMBIAPEDRO MARCOS MIÑAMBRES SPAIN

PERFUMERIE GANDUR S.A. SENEGALPIESA BULGARIAPINNACLE PAKISTÁNPOLINAT SPAINPRACSA SPAINPRODUCTOS DE LA VID, S.A. SPAINPRODUCTOS FINOS DE ÁGAVE MEXICOPROMARC S.L. SPAINRAJSHREE SUGARS& CHEMICALS LTD INDIARAFAEL CRUZ CONCE S.A. SPAINRAFAEL VILLEGAS SPAINREVELANCE SPAINRODRÍGUEZ Y BERGER SPAINRON BERMÚDEZ REP. DOM.ROM PAMPERO VENEZUELAS.C. ALCOROM RUMANÍAS.C. AVIPO EUROINVEST RUMANÍAS.C. GERMANY SANKT PETERS. RUMANÍAS.C. TUNGAL METROU RUMANÍAS.C. VINAALCOOL ARAD RUMANÍASALAS Y SIRVENT S.L.. SPAINSÁNCHEZ MONTALVO S.A. SPAINSANIVO SPAINSCOTT ROGER&NIXON S.A. SPAINSEMINSA SPAINSOC. GEN. AZUCARERA ESP. SPAINSODEVI PORTUGALSOGABINI SPAINSOTRAMEG MARRUECOSSUCESOR DE HIJOS DE P. VELA SPAINSUCROMILLES COLOMBIASURANES SPAINTABORA S.A. SPAINTARCAL ARGENTINATARCOL ARGENTINATEQUILA CAZADORES MÉXICOTEQUILERA DON ROBERTO MÉXICOTHAY ALCOHOL COMPANY THAILANDIATEQUILA HERRADURA MÉXICOTEQUILA SAUZA MÉXICOTOLSA SPAINTRANSFORMACIÓN DE ADITIVOS SPAINTUCSUCO, TUY HOA VIETNAMU.S.F. BEKOX SPAINUNIÓN ALCOHOL. ESPAÑOLA SPAINUP- JOHN SPAINUTECO SPAINVATRON Y MAU FRANCEVDA. ESTEBAN BOZZANO SPAINVDA. FELIPE ESPINOSA SPAINVDA. GONZALO FERNÁNDEZ SPAINVDA. JOAQUÍN ORTEGA SPAINVINAGRES PARRA SPAINVINÍCOLA DE CHANTADA SPAINVINÍCOLA DEL OESTE SPAINVINÍCOLA MANCHEGA SPAINVINÍCOLA ZAMORANA SPAINVINTBASA SPAINVINUMAR SPAINVINURI SI BAUTURI HARGUITA RUMANÍAVIUDA DE CIPRIANO GARCÍA SPAINWESTIM RUMANÍAXAMAI MÉXICO

LEGEND(Modality)

Basic Engineering BIDetailed Engineering DIConstruction CErection ESupply SUSupervision of erection SECommisioning supply CMFeasibility study FS

CLIENT COUNTRY PROJECT MODALITY YEARPedro Domecq Colombia S.A. Colombia 2 Pot still for brandy distillation, BI-DI-C 1.997S.C. Germany Sankt Pretergurg Pr. Rumania Grain Alcohol distillery, vacuum process. Capacity. 15.000 lt/day. BI-DI-C-SE-CM 1.997Promarc S.L. Spain Metallic grills for security C 1.997S.C. Vinalcohol Arad Rumania Alcohol plant reform, from discontinued to continued. Capacity: 8.000 lt/day. BI-DI-C 1.997Global Trade GmbH Germany Isopropapol distillery plant. Capacity: 950.000 lt/day. TURN-KEY 1.997Transformación de Aditivos S.A. Spain Scrubber column for alcohol recovery. DI-C-M-CM 1.997Sotrameg Morrocco Alcohol fermentation plant for Molasses. Capacity: 30.000 lts/day BI-DI-C-SE-CM 1.997Destillerías del Penedés S.A. Spain Alcohol recovery by vent in sotrage tanks. Capacity: 1.000 m3 BI-DI-C 1.997Pedro Domecq Colombia S.A. Colombia 2 Pot still for brandy distillation, BI-DI-C 1.998Minaz Cuba Copper column for molasses liquor production. Capacity: 35.000 lt/day. BI-DI-C 1.998Westin Rumania Columns for grain neutral alcohol production using corn as feedstock.Capacity: 10,000 lt/day. BI-DI-C-SE-CM 1.998Vinuri si Buturi Harguita Rumania Pot still for brandy distillation. BI-DI-C 1.998Transformación de Aditivos S.A. Spain Multiple effect evaportor for vinasses depuration. 20.000 Kg/hr evaporated water TURN-KEY 1.998Alficsa Cuba Complete alcohol plant, vacuum system using sugar cane molasses as feedstock.Capacity: 90,000 lt/day. TURN-KEY 1.998Alita Lituania Pot still for liquor production, using corn as feedstock. BI-DI-C 1.998SC Alcorom S.A. Rumania Complete grain alcohol plant, vacuum system using corn as feedstock.Capacity: 15,000 lt/day. TURN-KEY 1.998Euroavipo Rumania Complete grain alcohol plant. Atmospheric pressure system using corn as feedstock. TURN-KEY 1.998Biotecnologías Aplicadas S.A. Spain Reactors plant reform. M 1.998S.C. Tungal Metrou S.A. Rumania Grain Alcohol distillery. Atmospheric pressure system. Capacity: 8.000 lt/day BI-IC-SE-CM 1.998S.C. Alcorom S.A. Rumania Heat recuperator from vinasses´s distillery for heating system. BI-DI-C 1.998Revelance S.A. Spain Reactor with agitator. Capacity: 2.000 lt BI-DI-C 1.999Cubalcohol Cuba Fertirigation system to reuse the vinasses from distillery. SU 1.999Alficsa Cuba Computational control process for completed alcohol plant. Predicted adapted system. TURN-KEY 1.999Sotrameg Morrocco Heat recuperator from vinasses´s distillery for 535.000 kcal/day boiler BI-DI-C 1.999Casa Cuervo Mexico Distillery for agave liquor (tequila). Production: 25.000 lt/day BI-DI-C-SE-CM 1.999Orendain Mexico Cooler system for agave fermentation. Capacity: 140.000 kcal/h BI-DI-C 1.999Sotrameg Morrocco Water treatment system for boiler. Capacity: 8.000 lt/hr SU 1.999Casa Cuervo Mexico Plant to extract agave juice by Diffusion for tequila production (500 Tn/day) BI-DI-C-SE-CM 2.000Marex Rumania Maize cooker for hydrolysis and sacharification. Volume: 37.5 m3 BI-DI-C 2.000Sotrameg Morrocco Adaptive predective digital distrBIuted control system, for alcohol distillation plant. TURN-KEY 2.000Sotrameg Morrocco Expansion for distillation columns. Capacity: 30.000 lt/day BI-DI-C-SE-CM 2.000Decoinsa Spain Evaporation and deodorization pilot plant for purines (200 kg/h) TURN-KEY 2.000Ingenio San Nicolas Mexico Installation project for fire protection BI-DI 2.000Agave Distillers South Africa Agave´s liquor (tequila) distillery. Production: 100.000 lt/day BI-DI-C-SE-CM 2.000Deulep France Anhydrous alcohol plant, molecular sieve. Production: 100.000 lt/day BI-DI-C-SE-CM 2.001Eurociencia S.A. Spain Biological digestor pilot plant, and water treatment plant by inverse oSEosis DI-C 2.001Tequila Cazadores S.A. Mexico Plant for agave juice extraction by diffusion for tequila production (400 Tn/day) BI-DI-C-SE-CM 2.001Tequila Herradura S.A. Mexico Plant for agave juice extraction by diffusion for tequila production (400 Tn/day) BI-DI-C-SE-CM 2.001Tequilera Don Roberto Mexico Plant for agave juice extraction by diffusion. (400 Tn/day) TURN-KEY 2.001Biotecnologías Aplicadas S.A. Spain Reactor-decanter BI-DI-C 2.001Productos finos de Agave S.A. Mexico Plant for agave juice extraction by diffusion for tequila production (200 Tn/day) BI-DI-C-SE-CM 2.001Lilly S.A. Spain Depuration plant for pharmaceutical resDIues. Turn-key. TURN-KEY 2.002Seminsa Spain Two 300m2 water tanks for fire protection DI-C 2.002S.C. Bere Spirt Turnu Severin S.A. Rumania Grain Alcohol Distillation Plant for 20.000 lt/day of pure alcohol. BI-DI-C-SE-CM 2.002Tequilera Don Roberto Mexico Distillation column for agave´s liquor (tequila). Production: 40.000 lt/day BI-DI-C-SE-CM 2.002Biotecnologías Aplicadas S.A. Spain Biological reactors. DI-C 2.002Agropac Morrocco Water treatment plant for boilers. SU 2.002Agropac Morrocco Essentials oils distillation plant BI-DI-C 2.002Xamay S.A. de C.V. Mexico Agave juice extraction plant by diffusion (200Tn/day) TURN-KEY 2.002Tequila Sauza S.A. de C.V. Mexico Agave juice extraction plant by diffusion (400Tn/day) TURN-KEY 2.003Revelance S.A. Spain Deposit with agitator. DI-C-M-CM 2.003Tucsuco Vietnam Complete plant for alcohol distillation. Capacity: 20.000 ñt/day TURN-KEY 2.003Xuan Loc Vietnam Complete plant for alcohol distillation. Using cassava as feedstock. Capacity: 20.000 lt/day. BI-DI-C-SE-CM 2.003Tarcol S.A. Argentina Extraction diffuser of tartrates, from grapes mash. Capacity: 400 tn/day. BI-DI-C-SE-CM 2.003Polifenoles Naturales S.L. Spain Polifenoles extraction plant. BI-DI-C-SE-CM 2.003Ettehadieh Company Iran Engineering for molasses fermentation and distillation plant Capacity: 20 000 lt/day BI-DI-SE-CM 2 003

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