In this project, a numerical model describing the reaction mechanism and the mass and energy transport in wood pyrolysis is studied. The applicability of the model in predicting actual biomass pyrolysis assessed by comparing the model to TGA experimental measurements. The comparison to experiments is done in relation to the mass loss characteristics of chips of varying sizes. The mass loss is of interest as it is a variable necessary in the coupling of reactor and particle models. Three reaction models were simulated and results compared to experimental data, namely, the reaction model developed by Park et al. [Combustion and Flame 157 (2010) 481-494], a simple multicomponent parallel reaction model, and a competitive reaction model. The model of Park et al. did not fit with the experimental data as it underestimates the char yield. The parallel reaction model, which is based on hemicellulose and cellulose decomposition to char and volatiles, also did not agree with the experiments even when fitting the parameters to the data. The downward trend of char yield with increasing temperature suggests there exists competition between the volatiles and char in wood pyrolysis. The proposed competitive reaction model which consists of a hemicellulose reaction to volatiles and a cellulose reaction to volatiles and char is in good agreement with the experimental data. The mass loss characteristics in the experimental temperature range is fairly predicted within reasonable accuracy.

Through air drying (TAD) enables production of premium tissue products with increased softness, absorbency and bulk. On the other hand, the energy consumption of the TAD process is considerably higher than for conventional tissue drying alternatives. Previous studies on the TAD process have indicated that the drying rate for low grammage sheets is independent of the flow of air through the sheets.   The objective of this work has been to investigate and quantify how drying times and drying rates for low grammage sheets are affected by the addition of external web heating in a TAD process. Moist Eucalyptus and softwood sheets with grammages ranging from 15 to 60 g/m2 were dried in a laboratory process by an air flow through them and an IR-dryer with a variable power output. During drying, pressure drop and air flow were measured and an IR-camera recorded surface temperatures which enabled calculation of drying times and drying rates.   Using the IR-dryer to dry sheets shortened the drying time with at least 20 % and up to 60 % compared to sheets dried without IR-heating. Both pulp types and all grammages showed a linear relationship between drying times and the amount of evaporated water. Mass specific drying rates however, were very high for low grammage sheets and decreased rapidly with increasing grammage. Especially for low grammage sheets the drying rate had a very strong dependency on the IR-power and increased significantly with every increasing IR-power level. This finding implies that heat transfer could be a limiting factor when drying low grammage sheets in the TAD process. Another interesting phenomenon was observed for all grammages of the Eucalyptus sheets. Through these sheets the air flow rate increased with increasing IR-power, something that was not seen at all for the softwood sheets.   To summarize, adding external web heating to a TAD process resulted in a positive effect on drying times and drying rates, especially for low grammage sheets typical for the TAD process.

Syftet med detta examensarbete var att öka reaktiviteten hos förhydrolyserad kraftmassa genom att använda tidigare förhydrolysat och svavelsyra under förhydrolysen. Först bestämdes den kemiska sammansättningen av två olika vedråvaror (Acacia crassicarpa och Eucalyptushybrider) för att observera och korrelera med förhydrolysprocessen. Därefter studerades effekten av att för förhydrolyskraftkokning använda vatten, förhydrolysat och svavelsyra med olika koncentration under förhydrolysen vilket korrelerades med avlägsnandet av pentosan, utbyte, viskositet, kappanummer och ljushet. Därefter valdes en av vardera syrabaserad förhydrolyskraftmassa att blekas helt till dissolvingmassa för bestämning av Fock-reaktivitet, vilket jämfördes mot den vattenbaserade förhydrolysen som referens. Den slutliga kvaliteten på de olika förhydrolyskraftmassorna studerades också. Detta examensarbete visade att användandet av förhydrolysat och svavelsyra kan ge högre Fock-reaktivitet jämfört med vatten under liknande processförhållanden. Däremot gav syrabaserad förhydrolyskraftmassa lägre utbyte än vattenbaserad förhydrolyskraftmassa. Syrabaserad förhydrolyskraftkokning gav även lägre pentosanhalt, lägre halt extraktivämnen och lägre viskositetsvärden. Förhydrolysatbaserad förhydrolyskraftmassa hade värden mellan de som uppvisades av vattenbaserade- och svavelsyrabaserade förhydrolyskraftmassor. Dessutom hade förhydrolyskraftmassor från Eucalyptushybrider högre Fock-reaktivitet, lägre pentosanhalt, lägre halt extraktivämnen och högre viskositet än förhydrolyskraftmassor från Acacia crassicarpa. / The worldwide demand for dissolving pulp has been increasing significantly in Asia which is majorly produced from prehydrolysis kraft pulping and most of the prehydrolysis kraft pulp are consumed in viscose rayon production. Thus, it is interesting to have research in the process of prehydrolysis kraft pulping to make it a cleaner and more sustainable production. One of the most important qualities of prehydrolysis kraft pulp in viscose rayon is reactivity, which can lead to less chemical consumption and lower production cost. The aim of this research project is to increase the reactivity of prehydrolysis kraft pulp by using prehydrolysate and sulfuric acid during prehydrolysis cooking. Firstly, the wood chemical composition of two different hardwood species (Acacia crassicarpa and Eucalyptus hybrids) were determined and correlated with the prehydrolysis kraft pulping process. Secondly, prehydrolysis kraft cooking using water, prehydrolysate, and sulfuric acid with different concentration during prehydrolysis were studied and correlated with pentosan removal, yield, viscosity, kappa number, and brightness. Later, one of each acid based prehydrolysis kraft pulping were chosen to be proceed to fully bleached dissolving pulp for determining Fock reactivity which was compared to water prehydrolysis kraft pulping as the reference. The final quality of different prehydrolysis kraft pulps were also studied. From this research project, it showed that prehydrolysate and sulfuric acid prehydrolysis kraft pulp improved the Fock reactivity as compared to water prehydrolysis in similar pulping condition. However, acid based prehydrolysis kraft pulping gave lower yield than water prehydrolysis kraft pulping. Acid based prehydrolysis kraft cooking provided lower pentosan and extractive content, but lower viscosity values. Meanwhile, the prehydrolysate kraft pulp had the intermediate values between water and sulfuric acid prehydrolysis kraft pulping. In addition, Eucalyptus hybrids prehydrolysis kraft pulping had higher Fock reactivity, lower pentosan content, lower extractives, and higher viscosity than Acacia crassicarpa. To conclude, the more acidic prehydrolysis increased Fock reactivity with lower pulp yield, pentosan, extractive and viscosity.

Lignin är en av de vanligaste naturliga råvarorna på jorden och finns mestadels i trä. Nuförtiden är valoriseringen av lignin en av processutvecklingarna för teknologier inom massa- och pappersindustrin. Denna utveckling syftar till att öka värdet av lignin. Traditionellt förbränns genererat lignin, känt som tekniskt lignin, som bränsle i sodapannan som en del av svartlutskomponenter, och denna praxis är används kontinuerligt inom massa- och pappersindustrin. Syftet med detta examensarbete är att undersöka det tekniska ligninet från två specifika träslag, Acacia crassicarpa (Acra) och Eucalyptus Hybrids (Euca), för att öka kunskapen om det tekniska ligninet och hitta lämpliga tillämpningar för dessa råvaror i framtiden. I denna studie isolerades lignin från svartlut som genererats från två olika kokningsmetoder, kraftkokning- och kraftbased dissolvingkokning (KP och DP). Karakteriseringsmetoderna inkluderade molekylviktsfördelning (THF-SEC), analys av ligninets funktionella grupper med fosfor-31 Nuclear Magnetic Resonance (31P-NMR) kvantifiering och ligninets trukturella elementanalys via Two-Dimensional Heteronuclear Single Quantum Correlation NMR (2D-HSQC NMR). Utbytet erhållet från kraftkokning (KP) och kraftbased dissolvingkokning (DP) visade inga skillnader för samtliga prover och resultaten visas inom samma intervall (cirka 0,06-0,08 g/mol svartlut). Molekylviktsfördelningen för KP och DP-kokning ligger fortfarande inom intervallet för kraftlignin Mw (1500-5000 g/mol) och polydispersitetsindex (PDI) för KP hade ett högre värde än DP för båda typerna av undersökta råvaror. För de funktionella grupperna hade Eucalyptus Hybrids högre -OH-halt än Acacia crassicarpa oavsett kokningstyp. 31P-NMR kvantifieringsdata visade tydligt att KP-Euca innehöll den högsta halten av  alifatisk-OH (1,4 mmol/g). DP-Euca hade den högsta halten C5-kondenserad (2,5 mmol/g), medan den högsta mängden Guaiacyl-OH identifierades i DP-Acra (1,2 mmol/g). Fingeravtrycket av kopplingarna som kvantifierades från 2D-NMR HSQC visade att KP hade högre β-O-4', β-5' och β-β' interenhetskopplingar än DP. Dessutom hade Acacia crassicarpa en högre andel interenhetskopplingar än Eucalyptus Hybrids för båda kokmetoderna. De högsta β-O-4'-, β-5'- och β-β'-kopplingarna detekterades i KP-Acra med 3,4 %, 0,5 % respektiv 4,3 %. / Lignin is one of the most abundant natural raw materials on Earth and is mostly found in wood. Nowadays, the valorization of lignin is one of the continual process developments for technologies in the pulp and paper industry. This development is intended to increase the value of lignin. In the traditional approach, generated lignin known as technical lignin is burnt as fuel in the recovery boiler as part of black liquor components, and this practice is still common in the pulp and paper industry. The objective of this thesis work is to explore the technical lignin from specific wood species, Acacia crassicarpa (Acra) and Eucalyptus Hybrids (Euca), to emphasize the knowledge about the technical lignin and finding suitable application for the mentioned raw materials in the future. In this study, lignin was isolated from black liquor generated from two different cooking methods, kraft and kraft dissolving pulp cooking (KP and DP). The Characterization methods included molecular weight distribution by THF-SEC, lignin functional groups analysis via Phosphorus-31 Nuclear Magnetic Resonance (31P-NMR) quantification, and lignin structural elements analysis via Two-Dimensional Heteronuclear Single Quantum Correlation NMR (2D-HSQC NMR). The isolation yield obtained from kraft cooking (KP) and kraft dissolving pulp cooking (DP) did not have drastic differences for all the samples and therefore the results are within the same ranges (around 0.06-0.08 g/mol of black liquor). The molecular weight distribution values of KP and DP cooking are still within the range of kraft lignin Mw (1500-5000 g/mol) and the polydispersity index (PDI) of KP had a higher value than DP for both types of raw material investigated.  For the functional groups, Eucalyptus Hybrids had the higher -OH content than Acacia crassicarpa regardless of the cooking type. The 31P-NMR quantification data showed clearly that KP-Euca was the richest in Aliphatic-OH (1.4 mmol/g). DP-Euca had the greatest amount of C5-Condensed (2.5 mmol/g), while the highest amount of Guaiacyl-OH was identified in DP-Acra (1.2 mmol/g). The fingerprint of the linkages that was quantified from 2D-NMR HSQC showed that KP cooking had a higher β-O-4’, β-5’ and β-β’ interunit linkages than DP cooking. Furthermore, Acacia crassicarpa had a higher interunit linkages percentage than Eucalyptus Hybrids for both cooking methods. The highest β-O-4’, β-5’ and β-β’ linkages were detected in KP-Acra with 3.4 %, 0.5 %, and 4.3 % respectively.

Massatvätt är ett viktigt steg i kraft-processen, då kokkemikalierna kan återvinnas och återanvändas i processen, vilket minimerar belastningen på miljön. Det är ett viktigt steg innan blekning av massan, då en låg kemisk syre-förbrukning (COD) är viktigt för att minska förbrukning av blekningskemikalier. Dessutom kan massatvätt även eliminera andra oönskade material, såsom metaller eller extraktivämnen. Syftet med studien var att utvärdera av tvätt-effektivitet av industriell massatvätt. Målen var att jämföra industriell tvättning med extensiv tvättning, att undersöka kvaliteten av tvättvätskor med analystekniker och att undersöka befintliga metoder för att beräkna tvätt-effektivitet. Den experimentella fasen var indelad i provtvättning och tvätt-serier, utförda med olika tvättvätskor, uppehållstider och industriell och extensiv utspädningsfaktor. Provtvättningen gav resultat som möjliggjorde det att utveckla tvätt-metoden. Resultaten för tvätt-serien visade att den extensiva utspädningsfaktorn generellt gav bättre resultat och en mer effektiv tvätt, och att en tvättvätska med en temperatur på 80°C generellt gav bättre resultat. Ljusheten påverkades inte av utspädningsfaktorn och kappanalysen visade en väldigt liten skillnad jämfört med originalmassan. Utvärderingen av befintliga metoder för att beräkna tvätt-effektivitet indikerade att alla undersökta metoder kunde ge felaktiga resultat, men beräkningarna tillsammans med andra metoder såsom COD, konduktivitet och med flera borde ge industrin en god indikation på tvätt-effektiviteten / Pulp washing is an important step in the kraft process, as it allows for the cooking chemicals to be recovered and reused in the process, which also minimizes the environmental load to the subsequent stages. It is also important before the bleaching plant, as a low chemical oxygen demand (COD) carry-over is important to minimize the consumption of bleaching chemicals. Furthermore, washing can also remove other unwanted materials, such as metals or wood extractives. The aim of the study was to assess washing efficiency of industrial washing. The objectives were to compare industrial washing with extensive washing, to investigate the quality of wash liquors using analytical techniques and to examine existing methods for calculating washing efficiency. The experimental phase was divided into trial washing and washing series, conducted with different wash liquors, residence times and dilution factors (DF). The trial washing yielded results that allowed for the washing methodology to be improved. The results from the washing series indicated the extensive DF in general gave better results and provided a more efficient washing, and that a wash liquor of 80°C gave better results. Brightness was not affected by the dilution factor and kappa number analysis showed that there was a very slight difference compared to the original pulp. The evaluation of existing methods for calculating washing efficiency indicated that all investigated methods could give inaccurate results, but that the calculations together with other methods such as COD and conductivity should give the industry a good indication of the washing efficiency.

Cellulose Nano Fibrils (CNFs) can be extracted from wood and other plants. These CNFs are expected to play a large roll in future materials owing to their interesting properties and biobased nature. In this project, dewatering of gels made from CNF by non-confined mechanical pressing has been studied. A CNF suspension was gelled by the addition of HCl at pH 2 to form gel cakes and then pressed mechanically. The goal was to find the pressure limits of the gel cakes for different starting concentrations, in weight percentage [wt%], of CNF to optimize the pressure used when dewatering CNF gels. The non-confined pressing was achieved via the useof a Zwick/Roell Torsion multi-axis testing system. Gel cakes were pressed until a pressing equilibrium was reached. Equilibrium was reached when compression was less than 0.01 mm per 100 seconds. Gel cakes were frozen with liquid N2, freeze-dried, and analysed with Scanning Electron Microscopy (SEM). The results observed from the pressing data showed that gel cakes with higher CNF starting concentrations could survive higher pressures. Using the highest pressure available, at the pressure limit, yielded both the shortest run time and the highest dryness content. SEM imaging showed that the compression of the gel cakes starts at the surfaces and continuous inwards through the bulk. The mechanical pressure creates sheets of CNF both vertically and horizontally. By plotting the starting concentrations vs applied pressure a limit map with pressure regions could be created. From the limit map further optimization can be achieved to shorten the dewatering process of the CNF gels.

Med den ökande trenden av process slutning inom massabruken, så har det indikerats att återvinningen av tvättvätska från de olika tvättsteg troligen resulterar i negativa effekter. Närvaron av olika komponenter kan påverka upplösningen av lignin genom att främja dess återdeponering på massan, och därmed påverka senare steg inom bruket. Denna studie fokuserade på effekten av tvättvätskes sammansättningen, pH och magnesiumjoners innehållet på ligninåterfästningen till fibrerna under brunmassatvätt. Projektets syfte var att finna nya relevanta insikter för dagens verksamheter. För den experimentella proceduren blandades massa- och vätskaprover erhållna från ett barrveds-sulfatmassabruk, relevanta lösningsmodifikationer genomfördes, och dessa placerades i ett vattenbad vid 90 °C. Därefter tvättades och separerades den resulterande blandningen. Kappatal och ISO-ljusstyrka användes för massakaraktärisering, samt UV-VISspektroskopi för tvättvätskor. En ytterligare procedur med alkalisk urlakning utfördes på massan för att identifiera den relativt svaga liginbindningen. Resultaten indikerade att högre ligninhalt och konduktivitet, lägre pH och högre MgSO4 koncentration i tvättvätskor ökar lignininnehållet i massan. Under proceduren identifierades en möjlig konkurrens mellan borttagningen av lignin från fibrerna och återfällningen. Genom att uföra studier på olika bruksvätskor, så påverkades flera variabler systemet samtidigt, vilket förhindrade identifikationen av den dominerande variabeln som potentiellt kunde justeras för att minska återdeponeringen. Det observerades dock att en tillsatts av NaOH i tvättvätskor kunde reducera lignininnehållet i massan, medans däremot en ökning av MgSO4 kunde ha negativa effekter. / With the growing tendency of process closure within pulp mills, recycling liquors into different washing stages was observed to result in likely negative effects. The presence of different components may affect lignin dissolution, by promoting its redeposition onto pulp therefore affecting later stages in the mill. The present study focused on the effect of washing liquor composition, pH, and magnesium ions content on lignin reattachment to fibres during brown stock washing. This project’s motivation was to provide new insights relevant for today’s operations. For the experimental procedure, pulp and liquor samples obtained from a softwood kraft pulp mill were mixed, relevant solution modifications were performed, and these were set inside a water bath at 90 °C. Then, the resulting mixture was washed and separated. Kappa number and ISO brightness were employed for pulp characterization, and UV-VIS spectroscopy for washing liquors. An additional procedure of alkaline leaching was performed on pulp to identify relatively weak lignin attachment. Obtained results indicated that higher lignin content and conductivity, lower pH and higher MgSO4 concentration in washing liquors increase the lignin content in pulp. A competition between lignin removal from fibres and reattachment was identified to be possibly occurring during the procedure. By performing studies on different mill liquors, multiple variables affected the system simultaneously, which hinders the identification of the dominant variable to be potentially adjusted for reducing the redeposition. However, it was seen that adding NaOH in washing liquors could reduce lignin content in the pulp, whereas an increase in MgSO4 could present negative effects.

Abstract The wood industries to this day use almost exclusively petroleum derived adhesives that are based mainly on the reaction of formaldehyde with urea, melamine or phenol. These adhesives have low cost and good adjustable properties which makes it hard for bio-based alternatives to compete. Phenol formaldehyde (PF), as an example of a synthetic adhesive, has been in use for over 100 years. In some parts of the world, legislation around formaldehyde is changing, and there is an increasingly voluntary awareness about the toxicity and unsustainability of formaldehyde. Industries realize that raw materials from oil is unstainable. The latter is currently a driving factor behind research on alternatives to amino based adhesives. Also, consumer interest in healthy and sustainable products, such as emitting less formaldehyde indoors, increases the need for bio based adhesives. Cellulose contained in plant cell walls is a renewable, abundant and nontoxic resource. During the last decades, many innovations have been achieved around cellulose and this trend does not seem to be slowing down. Cellulose shows excellent mechanical properties, high strength, high elastic modulus as well as having a low density. Research about cellulose reinforced adhesives has been increased the last years. This thesis studied the enhancement of phenol formaldehyde adhesive with Crystalline Nano Cellulose (CNC) at 5wt% and 10wt% loading levels for producing plywood boards. Indecisive results when using CNC higher than 3wt%, especially with PF resin, have been reported by other authors. In this thesis, European standards were applied. EN 314 was applied to test the panels shear strength. Three (3) treatment classes were selected, indoor room condition as well as pre-treatments 5.1.1 and 5.1.3. Other properties measured were modulus of elasticity, thickness swelling, formaldehyde emissions. Results showed a shear strength increase for all pre-treatment classes. 10wt% CNC mixture with phenol formaldehyde in water bath, pre-treatment (5.1.1) for 24h showed the highest increase in shear strength (+73,9%). The 10 wt% CNC mixture panels also showed the highest wood fibre failure of all panel types produced. A decrease in MOE has been observed with 10 wt% CNC compared to the 5 wt% CNC panels. Formaldehyde emissions tests were inconclusive, but since less PF was used, there was a general reduction in emissions. The 5 wt% CNC panels were superior in terms of modulus of elasticity and swelling and also showed improved shear strength.

This work describes three alternative processes for producing microfibrillated cellulose (MFC) in which pulp fibres are first pre-treated and then homogenized using a high-pressure homogenizer. In one process, fibre cell wall delamination was facilitated with a combined enzymatic and mechanical pre-treatment. In the two other processes, cell wall delamination was facilitated by pre-treatments that introduced anionically charged groups into the fibre wall, by means of either a carboxymethylation reaction or irreversibly attaching carboxymethyl cellulose (CMC) onto the fibres. All three processes are industrially feasible and enable production with low energy consumption. Using these methods, MFC can be produced with an energy consumption of 500–2300 kWh/tonne, which corresponds to a 91–98% reduction in energy consumption from that presented in earlier studies. These materials have been characterized in various ways and it has been demonstrated that the produced MFCs are approximately 5–30 nm wide and up to several microns long. / <p>QC 20120928</p>

Den fundamentala principen för tillverkning av papper är inte en särskilt komplicerad sådan. Men för att pappret skall erhålla specifika egenskaper blir processen alltmer komplicerad. Bland annat tillsätts olika typer av kemikalier och processen övervakas ständigt av olika system. Ett av dessa system mäter pH-halten i pappersmassan. Mätsystemet är dock utsatt för frekventa mätfel vilket medför en felaktig dosering av den koldioxid som används för att sänka pH-värdet. Detta kan slutligen ha negativ påverkan på papprets egenskaper. Syftet bakom arbetet är att mätsystemet ska bidra till en jämn reglering av pH och därigenom garantera jämn papperskvalitet. För detta arbete har en frågeställning och ett antal mål och delmål etablerats. De övergripande målen omfattar att etablera en statistisk modell över mätfel och beräkna eventuella ekonomiska besparingar. För att uppfylla mål och besvara frågeställningen måste en grunduppfattning byggas uppför berörda delar av tillverkningsprocessen, pH-värdets påverkan i processen, pH-sensorns mätprincip, mätsystemets utformning och rutiner som berör mätsystemet. Med denna grund undersöks uppkomsten av mätfel för de sex mätpunkterna. Detta utförs med två tillvägagångssätt: Sammanställning av lagrade historiska data och sammanställningar avprovtagningar utförda under kontrollerade förhållanden. De aspekter som undersöks är magnitud, frekvens och hur dessa förhåller sig till olika processrelaterade värden. En kalkyl för kostnader berörande mätsystemet upprättas även. Denna omfattar aktuella kostnader för koldioxid och underhåll. I resultatet presenteras en statistisk modell över mätfel, uppdelat på historiska och i närtid. Den historiska modellen visar, för samtliga behandlade positioner, en medelavvikelse på &lt;0,3 pH-enheter. Den min- och maximala avvikelsen kan däremot uppgå till &gt;0,8 pH-enheter. Modellen för närtid visar på kraftiga avvikelser för fyra av de sex behandlade systempositionerna, som relaterar både till papperskvalitet och ytvikt. Denna statistiska modell används sedan för att beräkna möjliga besparingar. Här påvisades att viss besparing fanns, både för koldioxid och för underhållskostnader. Slutsatsen för detta arbete är att ett mätfel existerar för majoriteten av de behandlade positionerna. Det har även kunnat påvisas ett samband med de undersökta processrelaterade aspekterna, men resultatet kan inte garanteras fullständigt. Med detta kunde även en möjlig besparing av koldioxid uppskattas vid bättre mätnoggrannhet. Besparingen uppgick till c:a 200 tkr, vilket i jämförelse med företagets omsättning endast utgör 0,075‰ av denna. / The fundamental principle for manufacturing paper is not a complicated one. However, for the paper to acquire specific properties, the process becomes increasingly complicated.Among other things, different chemicals are added, and the process is continuouslymonitored by various systems. One of these systems measures the pH-level of the pulp. This system is however constantly affected by measuring errors, which in turn leads to the incorrect dosage of the carbon dioxide used to lower the pH-level. This could in turn have a negative impact on the properties of the final paper. The underlaying purpose of this project is for the measuring system to ensure an even regulation of pH and therethrough guarantee an even paper quality. For this project, several question at issue, goals and subgoals have been established. The general goals cover establishing a statistical model for the error and estimate possible economical savings. To fulfil the goals and answer the questions at issue, firstly a basic understanding must be established for: concerned parts of the manufacturing process, the effect pH-level has on the process, the measuring principle of the pH-sensor, the design of the measuring systemand the routines concerning the measuring system. With this basis, the occurrence of measuring error is examined for the six measuring points. This is accomplished with two methods: The compilation of historical data and the compilation of manual measurementsexecuted under controlled conditions. The aspects examined are magnitude, frequency and the relation to process related values. Finally, a calculation for costs regarding the measuring system was established. This includes current carbon dioxide and maintenance costs. The result presents a statistical model for the measuring error, divided into historical and near time. The historical model shows that for all the addressed positions, a mean deviation occurred &lt;0.3 pH-units. However, the minimum and maximum deviation could reach &gt;0.8 pH-units. The model for near time shows significant deviations for four out of the six covered positions, which in turn shows relations to both paper quality and surface weight. With this statistical model possible savings were calculated. This in turn showed the possibility of savings for both carbon dioxide and maintenance. The conclusion for this project is the existence of a measuring error. Also, a connection between this and the process related aspects could be established. Although, the result cannot be completely guarantied. With this, possible savings through better accuracy could be estimated. Though, these were only in the size of 0.075‰ of the company’s total revenue.