Mark Betz & Christine Betz

United States Tax Court·Decided July 6, 2023·No. 21587-18·Unpublished

Opinion

United States Tax Court

T.C. Memo. 2023-84

MARK BETZ AND CHRISTINE BETZ, Petitioners

v.

COMMISSIONER OF INTERNAL REVENUE, Respondent

DENNIS LINCOLN AND JULIA LINCOLN, Petitioners

v.

COMMISSIONER OF INTERNAL REVENUE, Respondent

[*2] Held: For all 19 projects, Ps failed to carry their burden of establishing that the products were pilot models. Accordingly, C’s purported qualified research expenditures (QREs) for costs of production failed to satisfy I.R.C. § 41(d)(1)(A) and were not creditable.

Held, further, for all 19 projects, Ps failed to carry their burden of establishing that the wages of certain of C’s employees were incurred in connection with the performance of qualified services. Accordingly, C’s purported QREs for wages were not creditable.

Held, further, for five of the projects, C did not retain substantial rights in the results of its research under its applicable contracts with its customers. Accordingly, C’s purported QREs for those five projects were incurred in connection with funded research within the meaning of I.R.C. § 41(d)(4)(H) and were not creditable.

Held, further, Ps are liable for accuracy-related penalties under I.R.C. § 6662(a) for tax years 2014, 2015, and 2016.

[*3] petitioners, the groups of which include the sole shareholders of the S corporation, are entitled to a research credit of $501,531 for tax year 2014 and (2) whether petitioners are liable for accuracy-related penalties for tax years 2014, 2015, and 2016. We hold for respondent on both issues.

FINDINGS OF FACT

Some of the facts have been stipulated and are so found. The Stipulations of Facts and the attached Exhibits are incorporated herein by this reference. Petitioners resided in Illinois when they timely filed their Petitions.

I. Catalytic Products International, Inc.

Catalytic Products International, Inc. (CPI), was founded in 1969 by Erwin Betz. In 2014 CPI was a subchapter S corporation, with the shares owned equally (50%) by Erwin Betz’s children, petitioner Mark Betz (Mr. Betz) and petitioner Julia Lincoln (Ms. Lincoln). As of January 2, 2014, CPI’s board of directors comprised Mr. Betz, Ms. Lincoln, petitioner Dennis Lincoln, and Matthew Lincoln. In 2014 CPI used an accrual method of tax accounting.

Beginning in 1987, when Mr. Betz joined the company, CPI transitioned its business away from manufacturing catalysts for installation in air pollution control systems, instead becoming a designer and supplier of custom-built air pollution control systems, primarily catalytic and thermal oxidizers.

II. Oxidizer Basics

In 2014 CPI supplied both catalytic and thermal oxidizers, which each eliminate certain environmentally hazardous airborne manufacturing byproducts. We will refer to these byproducts as volatile organic compounds (VOCs) as a convenient shorthand. 2 Catalytic oxidizers are designed to convert VOCs into carbon dioxide and water vapor via a process of chemical reaction between the VOCs and a

2 Our use of the term may not necessarily reflect whether the byproducts

discussed herein are VOCs within the technical meaning of regulations issued by the Environmental Protection Agency (EPA). See 40 C.F.R. § 51.100(s) (2023).

[*4] catalyst. 3 Thermal oxidizers are designed to achieve the same result but do so by using a burner to generate extremely high heat to incinerate VOCs, rather than using a catalytic conversion process. There are three separate subtypes of thermal oxidizers: (1) direct/straight, (2) recuperative, and (3) regenerative.

A direct/straight thermal oxidizer uses a simplistic burner to heat a combustion chamber; process air containing VOCs passes through the system and oxidizes when encountering the high temperatures. A recuperative thermal oxidizer adds to the concept by using a stainlesssteel heat exchanger to preheat process air, which provides for increased energy efficiency. 4 This heat exchanger usually consists of a shell and tube structure that operates by intaking clean, postcombustion air into an exterior shell that transfers heat to interior tubes carrying the process air. A regenerative thermal oxidizer instead uses a heat exchanger comprising ceramic media beds, which retain heat at an even higher rate and thus allow for increased energy efficiency. Regenerative thermal oxidizers operate by intaking process air through the media, then reversing the postcombustion air back through the media, thus retaining the heat. Because of their energy efficiency, the issue of overtemperature, where the system’s temperature rises too high and degrades the heat exchanger, is a particular problem for regenerative thermal oxidizers. Designs of regenerative thermal oxidizers typically use a hot gas bypass, which diverts high temperature air out of the system in order to reduce temperature. As of 2014, regenerative thermal oxidizers were the most common type of oxidizer used in manufacturing industries.

A few general considerations go into the choice of a type of oxidizer system and its basic design. One consideration is the aforementioned energy efficiency: Oxidizers can use considerable volumes of natural gas in operating the burners that heat the air. For cost-conscious customers, an oxidizer with reduced volume or performance but increased thermal efficiency (i.e., where high

3A catalyst is a substance that triggers a chemical reaction but is not itself consumed in that chemical reaction. A common example is the catalytic converter in an automobile, which converts the VOCs present in the exhaust into carbon dioxide and water.

4 To illustrate the concept, heat exchangers are typically used as part of the

heating process in residential gas furnaces. Furnaces use a burner to generate hot gas within a heat exchanger chamber; cold air then encounters the now-heated outer walls of the heat exchanger and becomes hotter before being distributed throughout the residence.

[*5] temperature is maintained without significant use of fuelconsuming burners) might be optimal. Another basic consideration is the concentration and type of VOCs generated by the customer’s manufacturing process; for certain VOCs, a catalytic reaction is less effective than a thermal one or would degrade the catalyst over time. Certain types of VOCs may also require a higher operating temperature or residence time to oxidize, which would affect the sizing of components and increase upfront costs.

Another consideration is whether the customer’s manufacturing process airflow contains other particulates or chemicals that could affect the oxidizer’s performance. For instance, if the process airflow contained silicone, oxidization would generate silicone dioxide (i.e., sand), which could accumulate and plug an oxidizer. Finally, the location and layout of a customer’s manufacturing process plays a role. Space constraints at the facility may dictate the choice and sizing of various components, while extreme temperatures or heavy winds may require additional insulation or structural support features for outdoor components.

III. CPI’s General Process

In 2014 CPI’s business model was as follows. First, CPI would either solicit or be contacted by a prospective customer. If unfamiliar with the customer, CPI personnel would sometimes visit the customer’s facility to review their manufacturing process and measure what VOCs were being generated. Customers would often provide CPI with the necessary specifications about the process airflow at the customer’s facility, such as the volume of process airflow, the type of VOCs generated, and the airflow temperature. If the customer was unable to provide specifications, CPI personnel or a third party would sometimes test and measure the airflow at a jobsite.

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