Refinery Gas Formula

[Danny Hosford]

Witha unique blend of high-quality ingredients, including mint, charcoal and aloe, this formula delivers powerful benefits for your skin. Mint works to soothe and cool the skin, leaving it feeling refreshed and energized. Charcoal draws out impurities and toxins, unclogging pores. Aloe nourishes and hydrates, helping to protect and repair the skin for a healthy, youthful appearance.

Learn more about the key ingredients.

Water, Sunflower Seed Oil, Kaolin, Potassium, Cocoate, Glycerin, Walnut Shell Powder, Apricot Seed Powder, Cetyl Alcohol, Glyceryl Stearate Citrate, Stearyl Alcohol, Bentonite, Aloe Barbadensis Leaf Juice, Anthemis Nobilis Flower Extract, Cananga, Odorata Flower Extract, Orange Peel Extract, Grapefruit Peel Oil, Melon Fruit Extract, Cucumber Fruit Extract, Elettaria Cardamomum Seed Extract, Jasmine Flower/Leaf Extract, Lavender Flower/Leaf/Stem Extract, Mentha Arvensis Leaf Oil, Apple Fruit Extract, Rose Extract, Raspberry Fruit Extract, Sandalwood Extract, Caprylic/Capric Triglyceride, Jojoba Esters, Tocopheryl, Acetate, Glyceryl Undecylenate, Glyceryl Caprylate, Xanthan Gum, Menthol, Sodium, Carbomer, Stearic Acid, Caprylhydroxamic Acid, Charcoal Powder, Glyceryl Stearate, SE, Caprylyl Glycol.

How to use?

Use once or twice a week. Do not use it on sensitive, peeling or compromised skin. Avoid eye contours and contact with the eyes.

To use as a scrub: Rub gently on wet skin and rinse with warm water before applying moisturizer.

To use as a mask: Use once or twice a week on thoroughly clean, dry skin. Apply evenly across the face using fingertips, avoiding the eye area. Rinse thoroughly after 5 minutes with lukewarm water.

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Great cleanser and exfoliant that doesn't dry out my skin.

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There is definitely a reason this scent went from limited edition to always avaliable year round. It's light and fruity and the perfect balm for summer...or year round. The watermelon and cucumber combination just feels like everytime you wear it you've taking a trip to the spa. Of all the balms I've bought, this is my trusted go to.

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The first two numbers represent the last two digits of the calendar year produced. The last three numbers represent the day of the year the product was packaged. E.G. 19134 would be the 134th day of 2019.

Refinery and Recalcitrant Organics is a highly effective blend of bacteria and nutrients designed specifically for difficult-to-treat wastewater streams from petrochemical refinery operations and other industrial processes that produce difficult-to-degrade (recalcitrant) organics.

I thought I had the formula figured out but my result calculations aren't lining up with what is actually happening. We pretty much all know that cooling Iron with Crude Oil raises the oil by just about 79.5 degrees C (91.8 to 171.3 in my most recent check). My problem is figuring out the formula that gives this number.

What am I either missing or getting wrong? Refining 100kg of Iron generates 67.1kJ (kDTU?) of heat according to the tool tip. Because there's 4 times the amount of coolant as refined metal, we can just divide the 67.1 by 4 and then apply the 1.69 Specific Heat of the oil to it, yes? Obviously I have this wrong since I'm calculating an increase of only 28.4 degrees C...

Working backwards I get a different result that is off by almost exactly 8 times. 79.5 degree change is 134.4 DTU/g, thus 53.742 million DTUs. This is basically 8 times the 6.71 million DTU that 67.1kDTU applied to 100kg of Iron equates to.

In this case, I can guarantee that all aspects functioned properly. This was a brand new refinery with oil straight from the bottom of the map and only a single order on the newest preview build. 800kg of Crude Oil along with the 100kg of Iron Ore was loaded in properly. 400kg of that coolant was moved into a separate section within the refinery as soon as the work errand was assigned. (The visible fill level on the refinery itself dropped to half and there were 2 separate lines in the "Contents" with 400kg each)

Then the "main tank" was filled back up to 800kg while the dupe was running the refinery, resulting in 1,200kg being held in the refinery. Once the job was finished, the 400kg part that was originally set aside changed temperature and was output.

As an aside, I don't remember the 400kg being set aside and another 400kg being loaded into the refinery while it is running. In fact, at one point after the initial order, I had oil flowing both into and out of the refinery while a dupe was using it. So they may have finally gotten a handle on that bug. >Crosses his fingersEdit: Looks like I confused some things here. I don't understand why the tooltip shows 67.1kDTU. Such amount of heat will increase 100kg iron temperatue by less than 1oC. So why it shows only 67.1kDTU?

Final temperature in the calculator calculations is not exactly 171oC as probably some heat is spread to refinery surroundings, but is still pretty close. I guess that also this 400kg of heated crude oil interacts with the other 400kg of still not heated oil so it can lower the final temperature.

EDIT2: actually the calculator has no use here. Better to just count heat generated by melting a given ore and take 80% of that value and then calculate by how much such heat will change temperature of a coolant.

Bottom line is, considering you said tooltip gives kJ, it's seems like it hasn't been updated for quite a while. The wiki values seem to be in line with the observed temperature change and you are correct it is 80% of the heat of cooling iron from melting temp to 40C

No, I have been using Polluted Water for all my Refinery needs in SI, which also included several tons of Steel and even in Rocketry, I might have been using clean water instead however they have the same SHC (since Expressive? Well, does not matter) but never did it overheat. The supply in SI has been 40C at least.

which sure is vague, quite possibly referring to a bug which may more or less frequently occur. It is still a matter of fact that one can see in SI that the added heat is the very same as it is now..Those are not new values but old values which the gamepedia had since long.

No, not quite if you are referring to the temperature change being 32,1, there is just a very high chance that the result will be rounded down instead of up especially for Iron (or mayhaps the game never rounds up so that one has to reach the threshold of 0 instead of 5). In the thread linked I actually tested myself and had Copper and Gold 0,1 hotter than Sam.

Obtain valuable Hydrogen and oxygen (indirectly) demand intel, Understand a refiner's required over the fence purchases, Gain insight into the hydrogen intensity per barrel for each refinery, and determine total hydrogen break-even price values, Spot hydrogen pricing values and scenarios ...

Equips users with the ability to model hydrogen production costs. Empowers users with global hydrogen intel that includes: new projects, global spot pricing trends, outages, refining hydrogen intensity and carbon emissions.

We have just about 700 refineries configured in our database. Users can currently select all US and Canadian complex refineries (simple upgrader refineries require a special case run from a customer support staff member). For other refineries please contact a representative at Refinery Calc for further assistance.

Heavy, sour crude coking margins-and not the economics of the few remaining cracking refineries-have had a more significant effect on the economic performance of the US Gulf Coast refining industry in recent years. The traditional 3-2-1 crack-spread formula, therefore, has lost much of its historical utility as an indicator of the economic performance of the refining industry as a whole, and coking refineries in particular.

One can also apply the coking-spread formula to refineries outside the US Gulf Coast. The pricing concepts are generally valid and one can select crude and product prices tailored for a particular market.

In the US West Coast-California market, for example, one can select product prices based on California Air Resources Board specifications and possibly Alaska North Slope or another crude for feedstock costs. Although the coking spread was designed for US Gulf Coast refineries, it can also serve as a accurate overall trend indicator of coking margins throughout the US.

The theory behind the crack-spread formula is fairly simple. It is grounded in the fact that refineries convert crude oil primarily into two key product classes: gasolines and middle distillates. Broadly speaking, demand for these two classes of products has a ratio of about 2 bbl of gasoline to 1 bbl of middle distillate.

When refinery analysts first started using the crack spread, West Texas Intermediate (WTI) crude priced at Cushing, Okla., was one of the most widely traded and price-transparent crude oils in the US marketplace. WTI-Cushing was a logical choice for the crude side of the crack-spread formula.

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